Author Archives: Gavin Brown

We are extremely proud to announce that PUMPNSEAL Australia were last week awarded Runner-Up in the Medium Business Category at the 2019 Business News Rising Star Awards

Thank you to the Business News Team for putting on another fantastic event this year, and also for recognising and formally acknowledging our solid growth!

We are honoured to be recognised amongst the best Medium Businesses in Western Australia and wanted to take the time to acknowledge our team members who all believed in the big targets we set a year ago, our customers for their continued trust, our suppliers for their services and our advisors for their continuous support and guidance.

Thanks to you all, PUMPNSEAL has topped an impressive year of growth and achievements with the implementation of our Workshop Automation Project, our nomination in the ANZ Business Growth Program, and the increase of both our turnover and our workforce.
We have grown beyond our expectations and are proud of what our amazing team of 27 people has achieved. This would not have been possible without our committed and long-serving staff and the culture within which we work together.

Our PUMPNSEAL team remains committed to investing for continued growth.  We have confidence in where we are heading and in our commitment to always provide our customers with the assurance of innovative, reliable and high-quality solutions.

January 2020 will mark 20 years in which PUMPNSEAL has been in business and we are looking forward to seeing you continue this journey with us for many more years to come.

The PUMPNSEAL Team

A customer was experiencing frequent gland failures on an Xstrata UFG 5000 Isa Mill™. Although it was a slow turning mill and low pressure, it was difficult to maintain a suitable seal with conventional gland packing. This was an acute and chronic maintenance event, impacting and causing a bottleneck in production of the plant, representing an annual downtime of more than 85 hours.

 

A review was undertaken of similar failure modes affecting pumps throughout the mill which was followed by close liaison with PUMPNSEAL Australia to engineer a suitable mechanical seal solution. Based on the earlier success of operating Chesterton Split seals in slurry pumps in higher head applications it was considered worth a trial. A 360mm standard version of the 442 seal was installed when the mill was scheduled for regular maintenance. The initial installation which took 2 hours eventually resulted in the elimination of further seal and bearing failures due to water contamination.

Features and Benefits of using Chesterton 442 Mechanical Seals:

  • No Failures. Seal failures reduced to zero
  • Planned 18-month maintenance program to inspect mechanical seal
  • Reduced gland water usage
  • Increased availability has provided an additional 1600oz of gold per annum
  • A sustainable unit cost saving of $2.56/oz directly in the bottleneck (revenue stream)

.Click here to find out more about the Chesterton 442 Mechanical Seal

Click here to download this Case Study

A client in the Gold Mineral Processing industry was reviewing the gland sealing life of their critical pumps in Tailings discharge and Cyclone Feed. It was found that the frequent gland failures and lack of proper adjustment of pump packing had a direct impact on the life of the pumps bearing barrels. Because of bearing failure due to moisture ingress, unscheduled pump refurbishment was frequent and in turn, caused the replacement of high cost wet-end components well before these parts (volute liners, impellers) had reached their full life cycle.

A solution was required to maintain an efficient seal and to control leakage to prevent further
bearing contamination.

Over a long period of time, trials were initially conducted with various manufacturers pump packings and gland flush control configurations. As this progressed with better benchmark data obtained, other options were considered to improve MTBR. In conjunction with PUMPNSEAL, a trial was offered with Chesterton’s 442 Split Mechanical Seals (7.00” and 220mm). The initial advantage was a mechanical seal that was split could be installed with out taking apart the wet-end of the pump. The runtime of the 442 mechanical seals with silicon carbide sealing faces and a Plan 32 controlled flush far exceeded everyone’s expectations. So much so, they have been adopted this technology on all the larger slurry pumps throughout the milling operations.

Features and Benefits of using Chesterton 442 Mechanical Seals:

  • No pump modification required and can fit directly to Warman and Krebs pumps
  • Runtime typically exceeds 15,000+ hours on 12/10 and 16/14 AH series pumps
  • No wear on the pump sleeve
  • No pump disassembly required to change seal faces or re-kit
  • Reduced gland water flush
  • Eliminates early replacement of pump liners and impellers

Click here to find out more about the Chesterton 442 Mechanical Seal

Click here to download this Case Study

Calpeda - PUMPNSEAL Australia Banner Logo

Blackmer® is proud and honored to be celebrating 115 years of unparalleled product performance, superior service and support, innovation, and a commitment to total customer satisfaction. This milestone is a tribute to the people, partners, and the products that have allowed Blackmer go above and beyond with our passionate commitment to innovative technologies that positively impact the world.

Before the turn of the 20th century, a rotary pump was generally understood to be a “gear pump,” consisting primarily of two meshing gears which trapped liquid between the gear teeth and the pump housing creating small sealing cavities that transported fluid as it rotated, forcing the liquid out the other side. But in 1899 R. M. Blackmer came up with a vane-type pump design that was an important departure from the old gear principle. In contrast to the flow rate from a gear pump that drops steadily as the gear teeth wear away, the loss from a vane-type pump is practically negligible. As the vanes wear away at the tips, they simply move further out of the rotor slots to self-adjust and maintain the original rate.

Blackmer CatalogBlackmer couldn’t have picked a better time to invent this ingenious type of pump. The advent of the automobile was giving the country a new thirst for gasoline and oil. The petroleum industry was growing by giant strides and the young firm was prepared to expand with it. The original Blackmer vane pump has fathered a family of hundreds of different pump models.

Today, Blackmer markets these pumps along with other fluid and gas technologies worldwide into a multitude of applications within the Process, Energy, Transport and Military & Marine markets.

Blackmer: The First 100 Years:

1899
Robert Blackmer invents new rotary vane pump technology that is the predecessor to today’s sliding vane pumps.
1903
Blackmer incorporates the Blackmer Pump, Power and Manufacturing Company in Petoskey, MI
1914
Blackmer becomes supplier to U.S. military.
1925
Blackmer relocates to Grand Rapids, MI, where its headquarters remain to this day
1950
Blackmer introduces integral mechanical seal
1954
Blackmer designs first liquefied gas pumps and produces first sliding-vane LPG pump
1964
Company is purchased by the Dover Corporation.
1968
Non-galling stainless steel pump introduced.
1980
First Blackmer reciprocating compressor introduced to the product line.
1987
ML4 pump introduced and outperforms gear pumps in viscous, high pressure applications.
1990
HD industrial compressors introduced.
1991
Company name changed from ‘Blackmer Pump’ to ‘Blackmer’ to reflect growing product line and single focused branding. Seal-less pumps introduced.
1993
Grand Rapids plant earns ISO-9001 certification.
1996
Purchased Hammond Engineering, a rotary vane compressor, hydraulic cooler, and screw compressor manufacturer in England.
2000
Acquires System One Pumps, an industry defining centrifugal pump that forced other competitive products to upgrade their pump designs.
2008
Blackmer joins Dover Corporation’s newly formed Pump Solutions Group(PSG™). Mouvex-Blackmer™ becomes an independent operating company within PSG. Other member companies include Wilden®, Neptune®, Almatec® and Griswold®.

The Rub with Wear Rings

Pumps with enclosed impellers normally have Casing and/or Impeller Wear
Rings, which are sometimes replaceable. Replaceable Wear Rings are usually an earmark of a more expensive pump style, and/or meets a higher specification, such as API 610. Material selection for the pump Wear Rings, and the proper clearances can make a big difference in the overall pump operation and reliability.

As a guideline, when specific OEM information is not available, choose the materials compatible for the specific service, and make sure that there is a difference of at least 50 Brinell Hardness between the Wear Ring materials. Most engineers prefer the softer material on the stationary Wear Ring.  If the Specific Gravity is less than 1.0, which is usually the case with hydrocarbons, it’s typically recommended to open the running clearances at least a few more thousandths than what the OEM recommends for running on clean ambient temperature water.

(Note: I personally recommend adding 0.003” more clearance for hydrocarbons SG less than 0.85.)

Thermal Growth Impeller Settings

When a stainless steel Shaft increases in temperature, it grows both radially and axially. The rate of growth is about 0.001” per inch of shaft for each 100 degrees F.  (0.01 mm per millimeter of shaft length per 50 degrees C rise).

Example: if a Shaft of 1.875 diameter and 20 inches in length was subject to 400 degree Fahrenheit temperatures, it would “grow” 0.080 inches in length and 0.0075 inches in diameter.

This can be enough change to contact the Casing (Volute). This is dependent on the final Impeller Setting and Casing/Impeller materials, as well. We mention this because unless you specify on the Purchase Order, the specific pumping temperature and request the Impeller be set at the appropriate clearance, the impeller will most likely be set at some lesser clearance. My personal philosophy is that the clearance should always be final checked in the field.

PUMPNSEAL Australia Relationship CalpedaPUMPNSEAL Australia are proud to announce their appointment as a distributor for Calpeda pumps in Western Australia.  Calpeda offer a broad range of compact End Centrifugal, Submersibles and Multistage Pumps suitable for variety of services from wastewater to fire. Have a try with their online pump selector , or make your job easier by calling our Pump Application Engineer with your next duty.

PUMPNSEAL Australia 2019 Calendar Photo CompetitionThe PUMPNSEAL Australia 2019 Calendar will soon be going to print and once again we would love our customers and staff to vie for the prestigious title of “PUMPNSEAL Photographer of the Year”. If you have taken an award winning WA coastal photo, worthy of featuring on our calendar, you could WIN a case of fine WA Wine along with the plaudits and applause of your peers in the industry.

Email a medium resolution image in Landscape format (less than 2mb for judging purposes), along with details on where and how you took the photo and with what equipment.

We will be accepting entries up until the 28th August 2018 and Judges decision is final!
Email your entry to: marketing@pumpnseal.com

So get those fingers snapping!

Packing friction plays an important role in the sealing of pumps and valves. Ideally, sealing is accomplished with the lowest practical frictional drag. Some frictional losses occur when the packing is compressed axially in the stuffing box to produce the radial contact that controls leakage. This radial load must produce a contact pressure on the shaft or stem and bore high enough to overcome the process fluid pressure. The equipment shaft, spindle or stem drive mechanism has to readily overcome static and dynamic or running friction during operation.

High packing friction can impede the equipment performance and efficiency by generating too much drag and heat. Excessive drag increases equipment power consumption and operating cost, and can ultimately result in equipment failure.

Figure 1. Typical stuffing box arrangements

Friction Definitions

Static friction occurs when there is no relative motion between the packing and the mating surfaces including the shaft or stem. This type of friction is prevalent in manual valves. With no relative motion, this higher frictional force must be overcome when motion is attempted.

Dynamic or running friction occurs during relative motion between the packing and the shaft, spindle or stem. This frictional force has to be overcome by these rotating or reciprocating elements.

Material

The coefficient of friction varies between packing materials. Some inherently possess a low coefficient because of the nature of the raw material. Graphite is one example of a material with inherent low friction characteristics. In general, PTFE has the lowest friction coefficient, with graphite not far behind. At temperatures less than 500-deg F, PTFE packing exhibits the lowest friction coefficient. The drawback is that it does not dissipate heat as effectively as flexible graphite. Flexible graphite and graphite yarn produce low coefficients of static and dynamic friction. Flexible graphite exhibits a friction advantage in both low and high-temperature applications. The combination of PTFE and graphite yields the best coefficient of friction: 0.15 to 0.05 for static and dynamic friction, respectively.

In some cases, end rings of braided graphite or carbon yarn packing or wire-reinforced braided packing are used as “wiper rings” to reduce friction by minimizing the build-up of graphite on the moving surfaces. They also work well to inhibit packing extrusion and help to support the radial whip of the rotating or reciprocating shaft/stem.

Number of Rings

Often, the number of packing rings in the stuffing box far exceeds what is necessary for sealing. Too many rings increase the contact area on the shaft/stem in excess of what is needed for effective sealing. As a result, the packing drag prohibits the shaft/stem from moving effectively, even if it is air- or motor-operated. A large number of rings generally increases the static or breakaway friction as well as the dynamic or running friction. The best practice usually is to use five packing rings and a solid carbon bushing to fill the rest of the stuffing box.

Figure 2. Packing radial pressure distribution

Packing Ring Cross Section

Square cross-section rings are used in the majority of dynamic applications. Cone-shaped moulded packing made of the proper density provides superior radial expansion capability at lower gland pressure, which may be one reason why cone-shaped packing performs with low friction in valves that cycle several thousand times an hour. Due to the narrow cross-section of some stuffing boxes, it may be difficult to design a cone or wedge seal to fit. Furthermore, if one is designed, it may be extremely difficult to install. While both the wedge and cone designs initially give low breakaway friction, studies show that there is little difference in running friction once packing consolidation is achieved. For quick turnaround and availability, square packing rings are more readily available and installation can be accomplished with less difficulty.

Lubrication

Braided packing friction can be reduced by the addition of suitable lubricants in the packing during the manufacturing process. However, these lubricants can be destroyed by excessive tightening of the packing or thermal decomposition from the operating conditions. Also, some chemicals can react with certain lubricants, causing the lubricants to quickly dry out and the packing to become brittle and abrasive to the shaft/stem. Using a clean external flush system will help cool and lubricate pump packing and reduce friction.

If pump packing has lost its lubrication from over-tightening, it is imperative to back out the gland bolt to allow the process fluid to leak around the shaft. This will provide lubrication and cooling between the packing and the shaft.

Conclusion

Excessive packing friction adversely impacts pump and valve performance and energy consumption, which translates to an increase in operating and equipment cost. Excessive packing friction may also increase equipment downtime due to packing failure and/or sudden equipment failure. Packing friction can cause major wear damage to the pump shaft or sleeve. It may also cause overloading of the equipment drive mechanism, which can cause overheating and damage to the pump or valve motors. The demand imposed at start-up by breakaway friction on the packed pump motor, air- or hydraulic-driven shaft/stem can be overwhelming. If the torque to overcome the packing friction exceeds the maximum power of the drive mechanism, it may cause catastrophic failure and may even cause harm to the operator.

To mitigate excessive compression packing friction, consider the following:

  • Use the packing material and design that will seal without generating excessive friction.
  • Ensure that the equipment is in satisfactory operating condition.
  • Employ additional cooling and lubrication by injecting lubricant into pump packing through the lantern ring.
  • Allow appropriate leakage of the fluid, at least 60 drops per minute in most pump applications, to provide a film of lubrication between the packing and the shaft.
  • Repack the equipment when the packing and gland are fully compressed if leakage is excessive. Do not install additional packing rings.
  • To control pump packing leakage, make gland adjustments at 15-minute intervals, tightening one flat at a time.
  • After installing pump packing and slightly hand-tightening the gland, start and stop the pump a few times before restarting.
  • Ensure that the packing width follows the rule of thumb of shaft/stem diameter to packing width ratio less than or equal to 4 (SD/PW ≤ 4), otherwise, the packing might not seal properly.

For more information on this topic see the following sections in the newly published FSA-ESA Compression Packing Technical Manual: (Copies are available from PUMPNSEAL) How packing works, Valve packing types, Pump packing types, Specialty equipment packing, Advances in compression.

PUMPNSEAL Australia Tamping Tools

Tamping Tools

Alan Ferris PUMPNSEAl Australia

Alan is a Senior Technician on PUMPNSEAL’s Pump Service Team. He is also a Land Rover/Range Rover enthusiast. Having driven Land Rovers in Cornwall in the open cast mines from the age of 17, Alan also competed in off-road trials about 20 years ago. He always dreamed of finding an early Suffix A 2 door model to restore, but they were very rare and hard to find in original condition. By chance neighbour’s friend approached Alan to ask if he was interested in his grandfather’s 1972 vehicle, which he had owned from new. Alan is now 15 months into the restoration project. It is important to Alan to retain the originality and character of the vehicle, so he is only replacing what absolutely needs to be replaced. “It would be lovely if the old fellow saw the project finished, but he is 102 years old, so it is doubtful this will happen at the speed I am going!” says Alan. It is clear that Alan is a perfectionist in his passion for Range Rovers and he brings this same attention to detail to his work at PUMPNSEAL!