Print page

Home » Overcoming slow, horizontal powder runs

Print page

Overcoming slow, horizontal powder runs

Q: We have a customer blowing our barite with SG 4.3 and ground to -75 micron, with around 16% -6 micron. While this material blows more quickly from truck to silo than Moroccan Barite with an SG of 4.18, ground to -75 micron, but with 25-30% -6 micron, on long horizontal runs it blows much slower on a horizontal run of approximately 100 feet from the silo to the boat. Is it possible that the higher SG and larger paticle size of our barite lets it settle out? What is normally the solution? Will using a smaller transport pipe raise the pipe velocity and overcome this problem, or can one just use a bigger blower?

A: It sounds like there is little horizontal line from the truck to the silo and the same blower is being used to transport the barite from the silo to the boat. Also, it sounds like this is intended to be a dilute-phase transport line. I suspect that the solids to air ratio is very high for both lines. While a solids-to-air ratio of more than 5 for this dense material would be acceptable in a vertical line, the dense material would have a higher saltation velocity than its choking velocity and could result in slug flow in the horizontal line. This system may require a larger line with more air flow, especially on the line from the silo to the boat to reduce the solids to air ratio and maintain the higher solids flow rate. As an alternate, the line from the silo to the boat could be converted to dense phase with the same line size, but you will need a high pressure blower. Calculate the solids to air ratio to see where you are. (Note: don't use blower capacity since in a pressurized system the leakage back into the silo and the lower blower output at the higher pressure result in much high solids to air ratios.) The 100-ft line does not appear to be long enough for this -75 micron material to settle. However, you may want to check the de-aeration rate. Take a large coffee can, fill it about 2/3 full, cover the can and shake it. Set the can on a flat non-vibrating surface and quickly remove the lid and throw a quarter on top of the material. If the quarter disappears, this material de-aerates too fast and will need to be conveyed in dilute phase at a solids to air ratio of less than 5.

Here are more of the latest questions on: Powder Handling

Can we use a centrifugal blower or root blower and what should be its capacity?
We want to lift Pet Coke powder ( 74 micron, density -0.7kg/m3, flow - average ) to a Silo 50 meters horizontal distance, 6 meters vertical distance with four 90-degree bends. Capacity required is 4 T/hr.

Can we use a centrifugal blower or root blower and what should be its capacity? We have to use bin vent filter, so what should be its capacity?

Is there a powder classification chart?
I would like to know if there is an available table or data available for conveying densities (pneumatic conveying) of powder/solid fuels such as coal, biomass (rice husk), woodchips, etc. In designing pipe lay-out, blowers and feeder valves, this data is important.

Can you offer short-distance pneumatic conveying solutions?
I'm new in solid handling and would appreciate your comments. Are there commercial products that can suck solid pellets (0.3 cm diameter from one box (4.5 ft X 4.5ft x 4.5ft) to a containers and/or hopper that are 6 feet elevation? The ideal tool would be a small vacuum device that can suck one product to a centralized area. This same device can swing several feet away to suck materials from another box to the same hopper.

Will an eductor driven by a blower work?

For powder handling, is there a system that ensures total protection of the product/environment?
We fill barrels from a dryer. The environment is a classic, non-protected chemical workshop -- a closed room where one production is in progress at a time.

Is there a system that ensures total protection of the product/environment and vice-versa? So that to control the particle and bio contamination of the product and ensure a safe handling for the workers. We're look for total closing and if possible an isolator.

How Can We Prevent Ratholing?
Working in a powder plant an investigation led us to define the problem of coreflow/ratholing causing weight fluctuations and segregation problems during emptying of the bin/silo. Designing a new bin we think about a conical bin with steep angles and short volume to try to avoid the coreflow. The powder characteristics are several small size particles and sticky characteristics so we fear polishing walls of the bin will not be effective in time. Placing a conveyor system for bin outlet will cause dramatic changes. A few hints for perfect bin angles and design would be appreciated.

Back to Ask the Experts

More content on this topic:

Featured Sponsor