Sunday, November 29, 2009

CENTRIFUGAL PUMPS – 2

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Continued from CENTRIFUGAL PUMPS – 1

HOW TO CALCULATE NPSH AVAILABLE:

The following parameters shall be considered when calculating NPSH.

a. Vapour pressure

b. Static head

c. Friction .

d. Strainer drop

e. Suction pressure

The empirical formula to calculate NPSH is

1. Assume some line configuration to get total equivalent lengths and convert that
in to friction drop.

 

Elevation in Meters

Elevations in Meters

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LS1 –LS2 LEVEL HIGH ALARM
LS3-LS4 LEVEL LOW ALARM
LS5-LS6 LEVEL LOW ALARM & TRIP OF PUMP
LEVEL SWITCH IS OF DISPLALER TYPE.
SETTING IS 70 MM BELOW THE LEVEL.

Proposed Location of Level Switches

 

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Thursday, November 26, 2009

CENTRIFUGAL PUMPS - 1

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Pump is an important rotating equipment which you will come across all type of industry. Pump section, performance. Installation of pump to get desired performance and connection of pump piping is very important for piping engineers. We can understand classification , working and standard engineers practice of pump from this article.

Terms to Remember :
Pump type, Head, Head loss , NPSH.

Sizing of centrifugal pump:

The centrifugal is like the ‘WORK HORSE’ in a process industry. The following figure shows major components in a centrifugal pump.

Sizing of Centrifugal Pump

Liquid is pressured in to the suction of pump where the impeller imparts a centrifugal velocity to the fluid. As the liquid discharges from the pump its velocity head converts to pressure head because of typical shape of the casing.

Pumps are usually specified early in the Process Schedule , when lines are ‘SKETCHILY’ located and sized when control valves have not been Sized and when pump performances must be estimated rather than established .

A complex relationship exists between the system head, Pump head and valve drop characteristics .Methods of selecting control valve drop and impeller performance are not readily Systematized .API-610 fixed many mechanical and procedural details and it is often included in all Refinery/Petrol chemical industries when pumps are specified.

A Design Engineer must consider two characteristics of a centrifugal pump., their discharge pressure and volumetric flow rate through them. The designer’s heat and material balance will give the required flow rate hydraulic Calculations will dictate the head.

1. HOW TO CALCULATE FLOW REQUIRED?

The kg/hr of liquid to be pumped is calculated from heat and material balance.

Case-1

Suppose we have a simple equation

HCL+ NaOH = = > NaCL + H2O
= = => (1 mole + 1 mole = = => 1 mole + 1 mole ) Mol. wts
= = => 36.5 kg + 40 kg = = => 58.5 kg+18 kg .

Hence for manufacturing 100 kg of NaCL you have to pump 62.40 kg of HCL &
68.37 kg of NaOH .

Case –2

Some times to take away the reaction heat , you’ve to add excess reactant .It may be as high as 5 to 6 times the actual requirement .

Case – 3

For some reactions , we have to keep some excess reactant to ensure
completion of (100 %) reaction.

Case – 4

As a design engineer, we have to consider about 20% flow as re -circulation to avoid cavitations problems in the pump.

Hence designed flow rate shall be 20% more than the actual flow rate. From
above pump flow ratio is calculated by following equation.

For example , if one has to pump 1000 kg/hr of H2SO4 (which has specific gravity
1.8 (98% H2SO4 ) , the required m3/hr is

II. HOW TO CALCULATE HEAD?

The figure on next page shows a typical process application.

The basic calculation consists of five components.

a. Differential pressure between two vessels.
b. Head to lift the liquid.
c. Friction head loss in the piping
d. Pressure drop allowed to Control flow
e. NPSH for the pump.

COMPONENTS CALCULATION

(a) Differential pressure:
To calculate the differential pressure I head, the following formula to be used.


Where Sp gr. is the specific gravity of the liquid pumped at the process
temperature.

(b) Head to lift the liquid

This is simply the difference between the liquid level in the first & second vessels.

(c) Friction head loss :

Actually a design Engineer does not lay the piping .Just consider that he can allow 0.3kg/cm2 Pr. drop for each other 100m of piping and estimate the approximate distance the piping will run . Double the calculated pr.drop to allow for elbows, bends, valves and other pipe fittings. Convert the friction pressure drop in to head by same formula.

(d) Control valves / instruments:

As a thumb rule , the loss across a control valve is equivalent to half the friction loss of pipe line or 1.50 kg/cm whichever is greater .

(e) NPSH required by pump:

NPSH required by a pump is normally given in the manufacture’s pump curve which is normally 0.5-4m .
As a summary , one can calculate the total pump head required for above pump
can be calculated as (sp.gr=0.8)

Some people may like it to play safe allow larger pr. drops in control valves and other instruments. This will lead to a bad selection of a pump where in sometimes you may get lower models of pumps.

Now we have arrived two basic requirements of selecting the pump that is Q & H(volumetric flow rate and head).

As in the case of turbines , specific speed is a sound design basis for a technical
classification of centrifugal pumps .

Specific speed is defined as the speed of geometrically similar impeller (pump)
when delivering one m3./sec against a head of 1 m.

Depending on the specific speed , the type of impeller can be selected from the following table:

Pumps having a specific speed less than 12 are generally not recommended. Infect the efficiency falls drastically if the specific speed is less than 20. This is because impeller becomes disproportionate, the dia. being too large relative to width.

It results in leakage and higher disc friction and fluid friction losses owing to narrow passage of fluid . It is therefore advisable to use impellers of small diameters consequently high specific speed.

This will reduce the disc friction losses which vary with the radius. The efficiency will rise & cost will fall in such case. Thus using higher stage pumps came in to picture.

If we select higher stages, H will be divided for that many stages and single impeller head reduce and Ns increases.

Depending on the blade shape, the efficiency changes and it can have one of the following different shapes.

image

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In order to have high efficiency, the blades bent backward shall be selected. Straight blades can be used for small pumps where economy is important. Blades bent forward yield very low efficiency and hence rarely used.

Selecting a pump’s impeller

The enclosed figure shows the typical set of curves, representing characteristic of an individual impeller .The top curve is for the largest size impeller that can physically fit in to the pump. Impellers are easily machined for any intermediate size between those indicated on pump curves.

-Never select a pump which requires maximum size of impeller, when selecting the size to avoid future modifications impossible .

Selecting a Pump motor

An experienced design engineer shall usually select a motor for centrifugal pumps based not on the size of impeller used but on the max. impeller dia that will fit in to the pumps .The reasons for selecting higher KW rating motors are :-

- It doesn’t trip for higher initial torque

- If engineer want to expand the pump capacity .

Otherwise the motor shall be selected at the end of the curve power OR with the following correlations as per normal practice depend on the absorbed power .

CONCEPT OF SHUT IN PRESSURE

SHUT IN pressure is the pressure the pump will put up at zero flow .The larger the impeller, the larger the shut in pressure . The max. allowable shut in pr. is the critical variable when selecting the size of an impeller.

The design engineer shall be assured that eventually the operator will block in a pump down stream.

For the illustration of importance of shut in pressure , see following figure.

If operator accidentally closes this valve , the shell of heat of heat exchanger shall be subjected to shut in pr. of the pump . In case HE shell is not designed for shut in pr. , we get three options.

a. Use small impeller

b. Install relief valve on shell

c. Eliminate valve

A design engineer ignores the consequences to downstream equipment when expanding the capacity of pump. The need to design all process equipment between pump and a block valve for the pump shut in pressure is a legal requirement.

HOW TO EXPAND PUMP CAPACITY

These are two inexpensive method to expand pumping capacity .

1. Reduce down stream pr. drop

2. Increase size of impeller

1. Reduce downstream pressure drop :

The typical causes of excessive pr. drop and suggested remedies are listed below , identified by many practical experiments .

a. High tube side pr. drop thro’ a shell & tube HE .

-Reduce no. of tube side passes

Going from 4 to 2 passes . pr. drop cuts by 7/8 ths.

b. High shell side pr. drop in a S/T HE

-A new tube bundle with larger spaces between baffles . (Expensive)

c. High pr. drop thro’ a wide open control valve

-change control valve port size or trim to the max. size permitted in the control valve body . e.g. 3” control valve can accommodate 2 port size .

d. Excessive piping Losses –

- Increase diameter of piping or parallel piping runs .

2. Large impeller :

The trick to select a larger impeller when expanding a pump capacity is to match the impeller size to the capacity existing motor drive. The changing of impeller is easy and cheaper when compared to changing the motor and its associate compounds .

The changing of the dia . of impeller is done thro’ following empirical relations .

To decide on the maximum size impeller that can be used existing motor , it is best to observe following in field .

a. Place the control valve position WIDE OPEN .

b. Measure amperage drawn by motor .

The rated capacity of the motor (in amps) can be multiplied by its service factor (typically 10-15 %). To calculate max. size of impeller that can be used with existing motor shall be

image

Where are is the rated amperage of motor including its service factor .

IMPORTANCE OF LOW DISCHARGE FLOW

When discharge of pump is closed .pump will overheat . The motor’s electric power is converted to heat as the pump churns the trapped liquid . The pump’s case and bearings become hotter and hotter and eventually the bearings will burn out also damage the pump seal .

In addition many large head pumps are subjected to a phenomenon called “internal recirculation”, which damages pumps internal parts when the pump is operated at reduced rate .

A simple modification in the process as shown below will automatically prevent pump damage due to low flow .

The designer should consider whether the min. flow by pass is necessary, considering the process variables of the plant designed .Never tie the min. flow discharge line in to the suction of pump .This defeats the purpose of line ; it must be routed back to a point in the process where the pumping heat is dissipated .

IMPORTANCE OF LOW NPSH

When a centrifugal pump loses suction due to low NPSH , the pumped fluid begins to flash at the eye of impeller .This results bubbles of vapors which when carried towards discharge are compressed and collapse. This phenomenon is called cavitations , which is a common cause for failure of pump .

A designer can prevent damage to many pumps by applying a few simple ideas .

a) Locate coolers on suction side of pumps .The decreased pump suction pressure will be usually more than offset by the reduction in the fluid’s bubble point .

b) Provide vortex breakers in bottom of all vessels regardless of the anticipated liquid level in vessel .

c) Provide adequate liquid hold in process vessels acting as surge drums . As a thumb rule 5-15 min. hold up is a typical range.

Continued to Centrifugal Pumps - 2


Monday, November 16, 2009

Design of Cross – Country Pipe Line - 1

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Introduction:

In the modern age of Industrial word, the Oil refineries, petroleum products, and petrochemicals form the major part of the industrial set-up all over the world. It is often economical and practical to carry the liquid and Gaseous products through pipe-lines rather than by Tankers over ling distance. When a pipe-line has to carry such products like crude oil, refined oil, chemicals like naphtha, ethylene, propylene etc. over long distance ranging from 10 km to even 1000 km,. Passing through land, rivers, sea, mountains, marshy areas, private and public land and land, rivers, sea, mountains, marshy areas, private and public land and crossing other services like roads, railways, transmission lines, underground Pipes/Cables etc, such a pipeline is called “Cross-Country Pipe-Line”. As the name suggests it transfers the liquid/Gas products from one place to another at far distance.

Engineering and Installation of Cross-Country Pipe-Lines form a special branch of piping
design and engineering., as it involves many aspects and parameter which are normally
faced with, in inplant piping system within the boundaries of refinery or a chemical /
petrochemical plant Special Techniques have to be adopted for design, laying
welding/jointing, corrosion protection, testing, commissioning etc. The most common line
familiar to all, is water-line from reservoirs to different consumption points, like, water-main from vaiterna/ Tansa dam to city of Mumbai Unlike water line, the hazardous chemical conveying Pipelines, involves many more stringent precautions in their design and installation. This is mainly due to fire and explosion hazards associated with the oils and chemicals.

This write-up highlights the main features of the eng ineering and construction of Cross-
Country Pipe-Lines. The objective of this note is to make the reader familiar with the broad perspective of the Cross-Country Pipe-Line Work and the pipe-lines which are already installed in India. These also include the submarine lines and en-land pipe-lines.

Advantages of Cross-Country, Pipe-Lines over transport by Roads / Railways / Waterways

The most common modes of transport known to all include Trucks running over Roads,
Railway goods train and Ships/Launches/Boats/Barges on waterways. The transport by Airway be cargo Air-crafts is also another way of bulk-transport. These modes of Transport have following limitations.

a) Availability of sufficient roads, rail-tracks and port-harbour facilities to take
up the traffic load.

b) Condition of the tracks.

c) Hurdles and conditions of the vehicles

d) Maintenance and conditions of the vehicles

e) Procedures and control involved in the Transport operation (permits/ licenses/octroi/toll/RTO etc.)

f) Manpower to run and maintain the transport system

g) Availability of fuel and power required to run the system.

h) Effect of Nature on the system like rains, storms, earthquakes, thundering, mist etc.

i) Pollution generated by the transporting vehicles.

k) Safety, insurance and security of the transported goods and materials.

l) Time taken for transportation and delays

m) Overall efficiency of the system.

While transportation by roads, railways, water and air-ways is widely used all over the world, it has its own limitations due to the features used all over the world, it has its own limitations due to the features (a) to (m) mentioned above. These limitations especially restrict or forbid their use when large quantities of Oil, petroleum, water, chemicals are to be continuously supplied from the source to the consumption point at users’ end. Hence the most reliable and efficient system can be provided only be Cross-Country pipe-lines.

The advantages are as given below :

a) Continuous un-interrupted transport is ensured.

b) No dependence on availability of roads, railways, bridges etc.

c) Least manpower requirement to operate the transport system except for inspection and maintenance of minimum required level.

d) No hindrances on way due to any reasons which are listed in problems (a) to (m) for surface transport, air/water ways.

e) Possibility of crossing any odd areas like seas, oceans, rivers, mountains and underground space.

f) Safety & purity of the product is ensured. The product reaches exactly in the same condition from source to the supply point, with minimal loss of quality or quantity.

g) Once laid down, the system works automatically especially with the help of modern instrumentation, safety devices, interlocks, communication system and remote control devices.

h) Minimum or no tampering on the way.

h) Cost of Transport per Unit of the product conveyed is far less than the transport by
Trucks/railways/ water/ Airways.

j) Fastest mode of transport even between two countries or continents.

k) Comparatively much less hazardous than surface transport & minimum dependence on human factors.

There are of course certain disadvantages but they are offset by the advantages, to a large extent, so as to make them ignorable as far as safety & techno-economic aspects are concerned. They are listed as given below :

a) Right of way Acquisition to run the pipeline, especially thru’ private & agricultural land
& habituated areas.

b) High fire & explosion Hazards potential.

c) Problem of corrosion & leakages & repair work involved.

d) Daily on-route inspection, testing & quick arrangements for attending to repairs and rectification work.

e) Possibility of laying other services in future (like other pipe-lines due to ignorance of
its existence, among other agencies) causing damage.

f) Special Techniques & Agencies are required to design, engineer, install & operate the pipe- line system.

g) Expensive cathodic protection required for the protection of u/g lines running in close
proximity of overhead High Tension electrical Transmission lines which induce the currents in the metallic pipelines, causing the corrosion by stray-currents.

The modern techniques are well developed to offset the effects of the above disadvantages. Even if a line has to shut-off for a day or two, the storage facilities at the users end take care of such stoppages even for 15 days to 1 month.

Preliminary work for A Cross-Country Pipe-Line Project :

The following necessary work on planning & collection of information/data is required to be for preproject activities, once it is decided to install a Cross-Country Pipe-Line.

Data on the Product to be carried :

- Name, Qty/day, properties of the product

- Source of supply & location details

- Names & location of consumers.

- Qty/day to be supplied to each consumer

- Storage facilities at suppliers’ end & consumer end

- Pumping facilities at Suppliers’ end

- Unloading facilities at receivers’ end

- Safety requirements for the product

- Risk& Hazards associated with product.

- Interruptions in supply at suppliers’ end & at receiving end.

Route Survey & Analysis

There may be many alternatives for routing the pipe line from supplier to the consumer. It is necessary to study the techno-economic comparison of the alternative routes. This survey includes the following activities :

a) Spot-level survey at every 50 to 100 metres & at least over 10 m on either side of the probable route.

b) Soil Conditions in the form of bore-logs, trial pits, chemical tests on subsoil & ground
water etc.

c) Alignment Map With lengths, bearings, angles etc. to know the exact route & the total
length of the pipe-line.

d) Details on the route and their locations dimensions etc sea, roads (crossing and along
side the route) rivers, Nallas, pipe-lines, bridges, rail-tracks, transmission lines, underground services including cables/pipes etc, Hills and mountains, buildings, plantation, forests, agricultural land etc.

e) Cadestral Survey –The route may be passing thru’ so many lands belonging to private
owners, farmers, govt. authorities, defence wings etc. En-route information and data has to be collected for such land pieces. Such data will include :

- Type of land and the owner’s name

- Length of the route thru’ the land.

- Problems in acquiring Right of Way (R.O.W.)

- Authority which will permit/grant Row

- Survey maps for the land available from the local Land Authorities (such as collector,
Tahasildar, Gram-Panchayat etc.)

- Land records regarding the title and ownership of the land

- Approx compensation required for acquiring the R.O.W.

- Status of Habitation on the land.

- Similar information of the adjacent plots on 50 to 100 m on either side of the route.

- Plans for future installations by others on the proposed route and/ or in the vicinity such as roads/ rail-tracks/ buildings/pipe-lines etc.

f) Availability of construction Materials, Labour & facilities

Since the pipe-line has to pass thru’ different areas and over a long distance, it is essential
to know the availability of construction Labour and Materials on the way. Such as excavation labour, transport facilities, access roads, construction material like stones, aggregates, sand, cement, steel, structurals, etc., workshop facilities. This information will be useful in working out project schedule and cost estimates and assessing the problems in construction.

g) Soil Resistivity Survey – required for design of cathodic protection system.

Names and addresses of the statutory and public bodies required to be contacted for
acquiring ROW, construction permission, blasting licences, excavating the public facilities
(Roads, rivers, rail-tracks etc.) and cathodic protection work, power supply/water supply etc.

Such authorities include the following but not limited to the listed ones.

  • Local land authorities – distr. Collector, Municipal corporation, Tahsildars, D.I.L.R. etc. Owners of the respective Land.
  • P.W.D. authorities – Local Office
  • Irrigation Dept.
  • Electricity supply Agencies/bodies/Boards.
  • Water-supply and Public Health Dept.
  • Controller of Explosives and use of Hazardous chemicals.
  • Industrial Development corporations
  • Railway Authorities
  • Marine and Port Authorities
  • Salt-commissioner and controller
  • Competent Authorities for Land and Row acquisition.
  • State and Central Govt. for necessary permissions, licences, clearances etc.
  • Import/export rules/ regulations authorities
  • Controller of Quarrying and Mining
  • Navy/Army/Air force (Defence Authorities)
  • Plants for future installations.
  • Forest authorities

Project Schedule

Base on various data collected as in 3.1 and the cost Estimates, over all project schedule
has to be prepared based on past experience, and specific problems unique to the project
under consideration. This schedule should cover only broad activities to serve as a guide
line for preparation of detail activity schedule.

This should generally include :

a) Preliminary Survey / Data Collection

b) Finalising the route

c) Cost Estimates / budget sanctions

d) Acquisition of R.O.W. and land

e) Basic Engineering package

f) Detail Engineering work

d) Construction work (Civil/Mech./Piping/Electr, Marine crossing, river crossing etc / cathodic protection)

h) Testing/Flushing/Pigging.

j) Commissioning and Hand over

This will establish the overall completion time for the entire project work.

Finalising the most optimum route

This involves the comparison of alternative router surveyed as in 3.1. The analysis should
include various parameters which are tabulated in the following format :

Under parameter columns, following minimum items should be included :

1. Estimated Cost

- Row Acquisition

- Land Acquisition

- Statutory Permission

- Basic Engineering

- Detail Engineering

- Material Procurement (pipes/Valves/Equipments)

- Construction Cost

- Civil

- Piping

- Mechanical

- Electrical

- Cathodic Protection

- On line buildings

- Marine / River Crossings

- Testing Commissioning

- Cathodic Protection

2. Overall completion – Time

3. Total length

4. Cost per km.

5. Other features

- Rock area (L)

- Marine Zone (L)

- No. of Road Crossings

- No. of Railway Crossings

- No. of Nalla Crossings

- Underground portion lengths

- Above ground portion lengths

- No. of Isolation Valves

- Pipe-line dia.

- No. of rectifier stations.

- No. of Diode Stations

6. Cost of operation / year

7. Cost of Maintenance / year

8. Hazard Classifications

9. Risk-Factor

10. Disaster Management Category

11. Stoppages / shut down due to ext. factors

12. Threat to Security and Safety etc.

Value analysis should be done for each alternative routes considering appropriate weightages assigned to these parameters and costs of the same. Thus final and most
optimum route can be selected.

Salient Steps in Detail Engineering

After deciding the final route, cost estimates, broad project schedule and engineering. The
detail engineering will involve following main steps.

Detail Design of each system

§ Civil works including trenching, sand filling, back filling, buildings, concreting, river-weights, valve-chambers, Test points, markers and construction infrastructure like site office, construction water, power, site godown/open yards etc.

§ Construction Equipment required for transport, laying, welding, erection testing etc.

§ Piping : Stringing/ Welding/ Laying/ Testing pipe support system

§ Catodic protection system design, diode stations, sacrificial anodes, UPSinstallations,
on-line test-points, insulation flanges

§ Specific designs for submarine portions and river-crossings

§ Designs of all crossings, pipe-bridges, supports

§ Preparing Detail Design and Fabrication Drawings for all Systems

§ Quantity calculation for materials and work items.

Implementation Planning and Organising

§ Selection and appointing Agencies/Contractors/Suppliers for various activities and
materials

§ Division of work among the staff on the project.

§ Progress monitoring and reporting system

§ Mobilising planning (manpower deployment planning) (Resource-planning)

§ Implementation work packages

§ Payment to subcontractor system

§ Inventory-control-planning

§ Safety/Security Guidelines

Organising Revisions/Change/alternatives/improvements in system design/drawing
during the project-process.

Preparation of As-Built construction drawings and final costing.

Data-Bank for the executed project, useful for future project.

Salient Features of Construction

Trenching : See. fig. 1

Generally Cross-Country Pipe-Lines are laid underground in an excavated Trench while
crossing the land-areas. Minimum depth of the Trench should be Trench while crossing the land-areas. Minimum depth of the Trench should be (1 M + Pipe dia + 150 mm). 1 M – is the depth of overburden i.e. back-filled soil, and 150mm is the thickness of sand cushion to be laid before lowering the pipe in the trench. Width of the trench is general minimum 1 M or as required by higher dia. Pipes. Thus width should be (Dia. Of Pipe + 0.4 M on either side) or 1 metre whichever is higher.

Minimum Trench Dimensions

Pipe-Preparation in Yard

- Inspection/Testing/Stacking of Pipes/Numbering

- Edge-Preparation for welding

- Wrapping/Coating (generally reinf. bitiminous) and its testing

- Testing/Stacking bends/elbows/Tees

- Pipe-Sleeves for road crossing

- Valve-testing/stacking/numbering

- Other accessories like blinds/spectacle blinds, gaskets, bolts, nuts, washers etc.

- Selecting/ Stacking welding machine/electrodes etc.

Stringing at Site and Welding

After trenching is ready over substantial length pipe-lines made ready in the yard as in 5.2
are transported to the site and lined up over sleepers placed across the trench for welding
and lined up over sleepers placed across the trench for welding the joints. The joints are welded continuously in 2 or 3 shifts. They are subject to inspection by D.P. check and Radiography. Wrapping/ coating is completed over portions about the weld.

Lowering

Once a fairly long length say 100 m to 150 m is welded/Tested, then if is lowered into trench over sand-bed already laid-Necessary small/big cranes, lifting tackles are used for lowering the line. Back filling with soft earth free from stones is done after lowering.

Hydrotesting

A long length after lowering a back filling is hydrotested for the test-pressure which is
generally 1.5 times the operation pressure or as stipulated for specific service.

Overall Total Welding

After each 100 to 150 m length is lowered, tested, then they have to be welded to form a continuous pipeline.

Testing of entire line is then taken up by filling the whole or section of line with water &
pressuring. Any leaks found are repaired and tested.

Pigging


For flushing and cleaning the entire length of all muck, dirt, welding rod bits etc, a pig is
passed thru the line, from one end, and it is pushed by water pressure. The pig travels
through the pipe, scrapping the muck and pushing it forward. At intermediate points flanged joints are left to pass-out the muck. If a pig gets stuckup, its location is detected by passing an ‘ISOTOPE’ and detecting its location by external instruments which tracks the isotope as it is travelling through the pipe. The pipe line is cut, pig removed, pipe cleaned and rewelded. The pig is passed through from that point onwards to flush the remaining portion in the forward direction.

Commissioning

It is done as per the procedure laid down for the specific product to be carried through the pipeline.

Cathodic Protection

This provides the protection to the underground pipe from the corrosion by electrolytic
process in subsoil water, whenever in e-m-f is induced’ in it (when pipe material is a good
conductor e.g. carbon. Steel)

Basic Principal and Phenomena

H.T. overhead Transmission lines conduct A.C. current under very high voltages of the order of 11 kv to 33000 kv and more. Due to fluctuations in voltage, magnetic field around the conductors also changes continuously. Any conductor in the magnetic field, thus cuts the magnetic flux and e-m-f is induced in it. (Ref. Fig). 2 below)

Induced E.M.F Phenomena

u/g pipeline of metal (viz. carbon steel) is a conductor of electricity. If it lies within the
magnetic field of electricity. If is lies within the magnetic field of the O.H. lines, then it
developes a potential higher than the ‘Ground’ potential. As we know, earth i.e. ground is at ‘Zero’ potential. When the u/g pipe is subjected to an induced e.m.f. if is supposed to be higher potential than the surrounding ground. The subsoil water always contains many
dissolved salts of sodium, potassium and other elements. This makes the subsoil also a
conductor of electricity. Thus the current flows from the pipe at flow of current depends on the resistivity of the subsoil. This phenomenon sets up an ‘Electrolytic’ process between the

pipe which acts as ‘ANODE’ and the ground which acts as ‘CATHODE’. Once this process
starts, pipe starts losing the positively charges ions say Fe++ or Fe++ into the subsoil
around the pipe. This is the corrosion process by which the pipe. This is the corrosion
process by which the pipe gives up its material & develops a hole or a reduction in
thickness.

Prevention of Effects of Induced EMF

To prevent this phenomenon, it is necessary to prevent the current from ‘PIPE’ to
“GROUND’. This is not possible, but it is possible to reverse the flow i.e. from ‘GROUND’ to ‘PIPE’. In other words pipe must act as ‘CATHODE’ and ground should act as ‘ANODE’.
This type of system is called ‘CATHODIC PROTHECTION’. In this case (ref. Fig. 3), the
current flows from ‘ground’ to ‘pipe’ and the pipe is said to be at –ve potential since the
ground has zero potential. The fig.3 is self explanatory. Applying a voltage by means of a battery set or D.C. current (rectified from A.C. supply or from D.G.) to the ‘anodes’ inserted in the ground surrounding the pipe and at regular regular intervals along the pipe This system, is maintained to see that the pipe always acts as ‘cathode’ then there are no chances of corrosion of pipe.

Current Flow from Ground to Pipe

3 – [Current Flows From Ground to pipe]

Diode Station in the Vicinity of Rail-Tracks with Electic Traction

The system described in 5.10.2, is often disturbed due to presence of other sources of
electric conductors in addition to the O. H. transmission lines, (e.g. Electric Traction). In this case, as shown in fig.4 stray currents flow from rails (which act as the path of return current) to the surrounding ground. This phenomenon, causes ground at-ve potential and quite often at lower potential than the pipe. This causes the flow of current from pipe to ground and the corrosion can take place. By supplying the current to a diode introduced in the circuit joining the rail to the pipe in such magnitude that the surrounding ground will conduct the current from ground to pipe,

Diode - Prevents the flow of current from pipe to ground

but not in the reverse way as diode acts like a ‘NON-RETURN’ valve. The calculations of
diode capacity, voltage to be applied etc. have to be made based on the survey conducted on fluctuations in the Traction field voltage. This arrangement prevents the pipe working as anode, but maintains it at cathodic level and thus prevents the corrosion.

Sacrificial Anode

In addition to the impressed D.C. current as in 5.10.2, sacrificial anodes are introduced into the ground, which maintain the pipe at lower potential than the ground, in case the D.C. supply fails for some reason. These anoces are made of Metals which are ‘NOBLET’ than the pipe materials. By this, it is meant that the metal which electrons surrounding or adjacent metals in contact is called a ‘NOBLE’ metal e.g. Mangessium (REF. FIG. 5)

Fig-5 Presence of Mg-Anode keep ground water at +ve potential water pipe

This makes the GR. WATER at + ve potential with respect to the pipe. Therefore the current flows from magnesium to the pipe. In this case magnesium Anodes slowly lose its own metal to the surrounding and in course of time dis This is why it is called ‘SACRIFICIAL’ anode periodically they have to be replaced by new anodes, say every 3 to 4 years.

Normal Subsoil Corrosion

Ever of there is no presence of Electric O.H. lines, or ‘Traction’ lines, any conducting metal
buried in the ground gets corroded by the similar phenomena. The subsoil water which itself is a ‘solution’ of so many salts, contains +ve and –ve ions. The presence of metal conductor such as ‘pipe causes movements of there ions and often the current from pipe to ground. This causes corrosion of the pipes which get electrostatically charged due to friction between pipe and the fluid flowing through it. Hence the sacrificial Anodes are required to be provided (Ref. fig. 6)

Fig-6 Normal Corrosion

On-Line installations

a) Test Points: Once the system of applying impressed current into ground to keep the
pipe at –ve potential, it is necessary to check the potential difference between the pipe and the ground at regular intervals, say at every 500 m. ‘Test points’ are installed close to the pipe. (se fig. 7) T.P. Box indicating voltage between ground and the pipe. Ground should be at least 1.5 v above pipe potential Volt-meter is carried by the inspector and the voltage between Terminals inside the T.P. Box is checked and recorded.

Fig-7 Test-Points at 500m

 

b) Insulating Flanges : If any portion of the pipe is above ground, then the same has to
be ‘Electrically Isolated’ from the under ground portion. This is required so as to prevent the flow of any other currents from sources outside and also the path of least resistance which the current may find through above ground pipe resting on steel or metal supports. (see fig. 8 on next page)

 Fig-8 Schematic Detials of Insulating Flange

All installations and systems described in section 5.10.1 to 5.10.6 from the Total System of Cathodic Protection.

Additional Information on Cathodic Protection (C.P.)

1.Necessity of cathodic protection is established on following criteria

a) Type of soil with its constituents like PH value, contents of chlorides and sulphates.

b) Soil resistivity which determines corrosion level.

c) Importance of line(s) to be protected.

d) Study of stray currents i.e. induction from EHV/HV lines, rail lines.

e) Dis-similar metals structures in the vicinity

f) Life of object to be protected e.g. 30/50 years

2.Two methods of C.P.

a) Sacrificial

Sacrificial is adopted for less important object & remotely located objects where electric
supply is not available early. Zinc, Aluminium & Magnesium are used as anode material.

b) Impressed current

Impressed current system is used for important objects and is dependent on electric power supply. Hi-silicon coast iron graphite are normally used as anode material for impressed current system.

3. Impressed current system comprises the following major equipment and accessories

a) Transformer Rectifier Unit

b) Anodes with tail cables

c) Anode junction boxes

d) Reference cell/electrode

e) Backfill material

f) Cables.

4. Criteria of selecting anodes and electrical equipment for buried pipelines.

Generally pipe lines which are buried, are buried, are coated and wrapped. This brings down the current level (and potential level) which is required to be provided. Generally 10 mA/sq. meter current criteria is used. For Pipe lines which are in sea water higher current upto 110 mA/sq. meter are used.

5. Following Data is necessary for engineering of C.P.

a) Dia meter of Pipe-line(s)

b) Length of buried pipeline

c) Material of construction

d) Type of coating.

6. Monitoring/maintenance of C.B. System

a) Potentials are measured on frequent basis (or daily)

b) Maintenance of electrical equip on periodic basis.

7. When construction period is long, during such period temporary cathodic protection has to be provided, until the permanent C.P. system is ready and commissioned.

Schematic Layout of A Typical Cross-Country Pipe-line 

7. Major Cross – Country Pipe Line in India

Major Cross – Country Pipe Line in India

NOTE: No. of crude oil lines (Submarine and Land) are in use for last several years, running between Gulf – Countries.

Continued to Design of Cross – Country Pipe Line - 2


Design of Cross – Country Pipe Line - 2

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Continued from Design of Cross – Country Pipe Line - 1

Additional Features about Piping

Pipe Thickness : The thickness is calculated in accordance with the standard methods and codes for different services and duty, including due corrosion allowance.

Anchor blocks at change of direction, made of concrete should be used to counteract the effects of outward thrust due to change in direction of fluid velocity.

If more than one pipe lines are running in parallel, minimum, clearance between the adjacent pipelines should be the largest of

(a) O.D. of the larger pipe dia over insulation if any

(b) 600 mm or

(c) as stipulated for specific requirement like working spacer for excavation/repairs, restrictions due to ROW space, adjacent features like road edge, building etc.

Surge Effect : Whenever the valve at or near the receiving end is shut-off, there may be
surge pressure effect on the pipeline as well as Pumps/Valves at the supply end. It is therefore necessary to decide the time-period for valve closing with appropriate communication between supplier and receiver. At times it may be advisable to introduce a surge tank or vessel at both the ends. This avoids the effects of ‘Fluid-Hammer in the
system.

Piping : When a multipurpose pipeline is used for carrying different products periodically,
pigging has to be done in addition to flushing and making the line ready for new fluid.

WHILE DESIGNING THE PIPE THICKNESS, THE FOLOWING ADDITIONAL FACTORE
SHOULD BE CONSIDERED SPECIFIC TO CROSS COUNTRY PIPELINES

PIPE-LINE supported on Brackets attached to a Road or Railway Bridge :

When a line runs along-side a bridge, the vibrations of the bridge due to Traffic Movement, are also transmitted to the Pipe-line. It is necessary to estimate the vibration-levels (frequency and Amplitudes) of the bridge. Generally these data will be available with the respective authorities or designers of the bridge. We have to check and prevent the natural frequencies of the pipe-line, matching with the exciting frequencies of the bridge, to avoid resonance effects. It is advisable to provide lateral spring-loaded supports at random intervals, to get damping effect and random frequencies. In case of railway-bridges, regular patterns of vibrations are more probable when the train is passing.

LONG EXPANSIONS LOOPS

As the line is exposed to out-side atmosphere, whenever it runs along the bridge-side,
thermal expansion and contraction take place due to Temperature variations. Generally a
long and wide loop is provided under the bridge as shown in fig. 10 structural behaviour of
short and long arms of the Loop will depend on the deflections and the stiffness of the arms.

Due analysis should be made to calculate the stresses induced in the pipe. Also note the
supporting arrangement of the pipe as shown in fig. 10. which has following main features.

§ The rollers are provided to allow free longitudinal movement of the pipe due to
expansion and contraction

§ Loose clamps are provided over pipe-line at intervals with 25 to 30mm gap allaround,
to prevent possibility of the line slipping off the supports due to long-length. (Long pipe-line behaves like a flexible wire and when expanded, may tend to moveout from the supports.

§ Lateral spring supports are provided at random intervals to prevent possibility of
pipe-natural frequencies matching with Bridge-frequencies.

Erection Stresses

The handling of pipes may induce local and excessive stresses in following conditions.

a) When cranes are used for lowering long lengths in position, local deformation/bending may take place.

b) When pipe is pulled along the trench or through the sleeve laid across the road.

c) When the sub-marine portion of the line is gradually lowered from water level to below the sea or river bed, it undergoes deformations at local points.

d) When long un-supported (un-back filled Trenches) lengths are hydrotested, the flexibility of long lengths, sometimes causes vibrating movements on micro-scale and
are more predominant than in case of small in-plant piping. These have to be correctly assessed or damped by intermediate Temporary and / or permenant supports, thrust blocks, anchors, backfilled portions etc.

e) When the pipe-line crosses a Hillock, it goes up the inclined plane and from peak runs down the slope. The up-going line is subjected to a sort of compression due its own weight due to sliding tendency or tension due to pulling effect, down the plane. The stresses due to any of these effects should be estimated and provided for.

CORROSION ALLOWANCE

In normal in-Plant piping, standard corrosion allowances are specified for various duties in
different design codes. Cross-Country pipe-lines run over a long distance and the leaks on
any account cannot be permitted. Hence extra corrosion allowance is specified for cross country pipelines. In any case minimum of 3mm or as specified, whichever is greater, is provided as corrosion allowance.

Design codes generally followed for cross-country piping (in addition to normal codes for all piping)

§ ASME B-31.4/ 31.8 for thickness Design

§ API – 1104 for welding and related tests specifically on cross-country Gas and Oil
lines.

§ API – 5L for material of construction

Generally, in non-hazardous fluid line, say water-lines. Breather valves (pressure and
Vacuums) are provided at he highest points, say on Bill-top, to prevent ‘Air-lock’ or to suck-in Air in case vacuum or cavitation takes place. But in pipelines carrying Gas or Hydro-carbon liquids like crude oil, refined oil, naptha, ethylene, propylene etc. No BRATHER VALVE is PERMITED any where on the line. This is because the hazardous liquid cannot be allowed to come out into the atmosphere and Air (which contains oxygen) cannot be allowed to be sucked-in as the fluid may combine with atmospheric oxygen and catch fire. Anytime the line is to be commissioned, the fluid to be carried is filled into the pipeline by first passing the pig from supply end. There are no chances of Air-Lock. In this case.

Cross-Country Pipe Line - Along Bridge-Side

Cross-Country Pipe Line - Typical Road Crossing

Cross-Country Pipe Line - Along Sea-Side

Cross-Country Pipe Line - Along Hill Side

SPECIFICATION FOR COATING AND WRAPPING OVER UNDERGROUND PIPESß

1 GENERAL SCOPE OF OPERATION

1.1 Cleaning / Scraping external pipe-surface

1.2 Priming with synthetic primer

1.3 First Coat of coal Tar Enamel

1.4 First layer of Inner Wrapping of Fibre-glass tissue fabric

1.5 Final Coat (2nd Coat) of Coal Tar Enamel

1.6 Outer wrap of coal-tar impregnated Fibre-glass tissue Fabric

1.7 White Wash

2 REGULATION

All materials conform to AWWA C – 203-86 or BS – 4164-1987 or ASTM Standards

3. LIMITATIONS

Coal-Tar enamel based coating-wrapping should withstand the liquids carried upto
Temperature of 60 deg C

4. INSPECTION AND TESTING

Applied coating/wrapping should be tested by SPARK TEST to be applied with HOLIDAY
DETECTOR Any sections found defective with pin-holes, cracks, internal hollows, pockets, wrinkles, airpockets, less thickness etc. should be removed redone and retested until they are made defects-free

5. HANDLING AND PLACING

The pipes already coated/wrapped should be carefully using special strap-type lifting clamps to prevent concentrated loads and forming dents or depressions. The straps shall be of flexible but strong and soft rubber sheet wide-enough to distribute the self weight of lifted pipes within the intensity which coating/wrapping can withstand without getting damaged or depressed.

SELECTION OF PROTECTIVE COATINGS FOR UNDERGROUND PIPELINES

Mr T K Roy, Vice President—Technology, STP Limited

ABSTRACT

Like the selection of pipe materials, coating materials for• protection of pipes vary depending upon various factors. The paper summarizes the basic needs for selection of
coating material for the long in service life of gas and liquid transmission system.

INTRODUCTION

It is most important to recognise that the coating material by itself will not result in
optimum corrosion protection of the pipeline. A total pipeline protection system includes
consideration of steel quality, coating application, surface condition and treatments, design of coating and Cathodic protection system.

Practical experience, as well as soil corrosion •studies has led to the conclusion that the
properties of soil are more important than the composition of metallic material in
determining the character and rate of corrosion. Soil corrosion tests are for this reason
concerned largely with determining the nature and predominance’s of the corrosive and
protective factors of those environments.

The elements of soil may be classified roughly as corrosive or accelerative and protective
or repressive. Relative concentration and composition of these two types of elements are
the determining factors for selection of pipe coating materials. The physical texture and
drainage of soils affects the concentration and availability of oxygen. Contact of soil
particles with metal surfaces gives rise to oxygen concentration cells and it is mainly by means of the operation of cells of this type that metal corrodes in soils. Pores and holidays and other imperfections comprise an important source of corrosion cells.

PREREQUISITE CONDITIONS FOR COATINGS

Surface conditioning:

Abrasive cleaning of the pipe surfaces to a white or near white blast quality is not
sufficient for a good coating operation as ill effects of chloride contamination is not
removed by this process. It has been established that most harm is done by the
presence of ferrous salts which is not removed by abrasive cleaning process or by
high pressure water’ blasting. The steel surface energy plays a critical role for
accepting coating material A non contaminated steel surface has a surface energy
higher than 73 dynes/cm2.

In normal condition even after blast cleaning the surface energy of steel surfaces
varies from 45 to 50 dynes/cm2 . In order to have a good wet ability the coating material should have a surface energy well below 45 dynes/cm2 (As per ASTM D
2578)., Another criteria for steel surface which is to be considered for selection of
coating material is its mixed surface potential (micro anodes arid cathode). In order
to overcome the surface anomaly it is necessary to treat the blast cleaned surface.
A chemically cleaned surface by removing the contaminants help wetting of the
coating effectively. Treatments with chromates and silicates or by using adhesion
promoter the surface potential of the steel surface can he made more uniform which reduces the driving force between anode and cathode, increasing resistances to electron flow and passivating the surface.

Adhesion:

Adhesion of the coating material is the most important factor while selecting a
proper material for steel pipes.

The adhesion is based on three mechanism~ mechanical polar and chemical adhesion.

Mechanical adhesion is achieved through physical anchoring of coating material in
the peaks and valleys obtained by blasting. This is not very strong in nature.

Polar adhesion is most widely occurring mechanism of coatings. The bond strength depend on the availability of polar sites on both the substrates and the coatings. Adhesion achieves the highest value when polar groups are in close molecular proximity. A good wetting of the coating satisfies this condition.

Though chemical adhesion gives the strongest bond, it is rarely used for protective
coatings of Pipe Lines, Chemical bond is achieved by functional groups on the substrate and coating interacting chemically; This is focused for Pipe Lines other than steel. Adhesion is extremely important against resistance to Cathodic disbondment. It has been found that the effects of electrolytes particularly, if sodium and potassium ions are present, can be very destructive in the interfacial bond under the Cathodic protection influence. This can lead to ineffective Cathodic Protection.

Type of Coatings:

Coatings can be classified as organic and inorganic and in many cases a combination of the two is used.

Coatings provide corrosion protection through passivation, barrier and sacrificial ways. Most pipeline coatings are based on barrier concept. Three types of organic coatings are in use for giving barrier properties Thermoplasts, Thermosets and Elastomers.

Thermoplast coatings are generally applied by hot melt technique and solvent evaporation technique. Examples are Polyethylene, Polypropylene, Nylon, PVC, Coal Tar Enamel and Asphalts. Common characteristics of these polymers are good mechanical properties and resistance to moisture but sensitive to exposure to high temperature.

Thermosets costing are formed through cross linking induced chemicals by hear, chemicals or radiation. Examples are Epoxy, Polyester, Phenolics which have generally good heat but resistance but relatively poor in mechanical properties.

Elastomers are classified as hybrid of the two. Examples are urethanes.

Selection of coating materials

In selecting a coating material the nature of the soil corrosion and the soil movement are of prime importance. Many materials pass the basic properties for the control of corrosion but only a limited number meet the overall needs of pipeline protection.

Correct selection of the products most suitable for the required duty from the range available is equally important taking into account the size of the pipeline, operating temperature, comprehensive site survey information relating to soil condition including resistivities, acidity, redox potential, presence of a sulphate reducing bacteria and the nature of the terrain through which the pipeline, route passes.

In the design of corrosion protection system for a burned pipeline and its subsidiary components, both coating and Cathodic protection system must be considered together.

As the coating for a pipeline is considered to be the primary method of corrosion control then it is to be decided which coating should be used for most effective method of protection in the environmental conditions appertaining along the total pipeline route. Essentially the Sating material must be stable for the required length of service for the pipeline under consideration and due regard must be given at th! planning stages to the choice of coating that will meet all the conditions of service.

In addition the coating must be totally compatible with the micro environment surrounding and with the Cathodic protection system.

Whatever may be the nature of the coating material, the effectiveness is corelated
with a number of technical characteristics which the protective coating must possess to a satisfactory degree. These may be classified as follows:

1. Be chemically inert to any corrosive agents present around the pipeline

2. Be resistant to the action of any micro-organism and bacterial degradation present in the environment in which the pipeline is laid, both aerobic and anaerobic.

3. Be resistant to marine organism for submarine pipelines, coating should not be easily penetrable by marine life such boners, barnacles.

4. Posses a high degree of electrical resistively, sufficient to ensure the electrical
insulation of the metal pipe from the laying environment.

5. Be highly impermeable to water and water vapour and shows negligible water absorption.

6. Be closely bonded to the metal, in order both to prevent the spreading of corrosion
under the coating in the case of local faults and to oppose the forming of moisture containing pockets at the metal coating interface, due to parting by mechanical actions or electrolytic effect of the cathodic protection.

7. Possess an adequate impact resistance, so as to allow the pipes to be transported
and handled without undue deterioration of the coating.

8. Be capable of withstanding the stresses induced by the soil in which the pipe is laid
and due to its physical and chemical nature and . resistance to considerable stress from soil movement such as contraction by clay during prolonged dry spell.

9. Have a service life atleast as long as that expected of the pipe to be protected, retaining unchanged its chemical & physical characteristics.

10. Suffer no alteration under the condition created by Cathodic protection (high
alkalinity, nascent hydrogen and nascent chlorine)

11. Be very easy to apply, avoiding the use of sophisticated technological processes,
complicated machinery and high cost, hard to replace skill labour.

12. Special technical characteristics may be required by particular environmental
conditions in the laying and operation of the pipeline to be protected.

13. Be flexible enough.

Moreover, in the choice of coating two economic conditions will have to be made:
ease of application and repair and an acceptable overall cost. The matter will include the cost of the coating material, of its application and repairs of any damage incurred in transportation and handling.

Among the recent development of coating materials the hybrid system of Coal Tar Epoxy, Coal Tar Polyurethane and rigid Polyurethane are in consideration. The hybrid system is aimed to reduce the shortcoming of both the individual material without increasing cost. Coal Tar Epoxy and Coal Tar Urethane are specially suitable for lower dia steel pipes below 12” where costly Fusion bonded Epoxy is mostly being used in some countries. Rigid PU system can go to coat bigger dia pipes but it is costlier than Coal Tar Enamel which is normally preferred material for pipes above 12” dia.

In FRE system also instead of using straight epoxy hybrid epoxy polyester system is under study.This hybrid system improves the short comings of straight epoxy system viz impact strength and mechanical resistance.


 

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