Thursday, November 20, 2008

Power in Human Cell Size Micro Battery

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Team led by associate director, Shuguang Zhang managed to use the energy generated by trees to power a network of wireless sensors (-Tree Power-), Professor Zhong Lin, Wang research group managed to generate power from Fabric (-Fabric Generate Power Caught Global Interests...-), and now MIT engineers led by professors Yet-Ming Chiang have developed a way to create and install tiny microbatteries, about half the size of a human cell and built with viruses which could one day power a range of miniature devices, from labs-on-a-chip to implantable medical sensors -- by stamping them onto a variety of surfaces.

In the Proceedings of the National Academy of Sciences (PNAS) the week of Aug. 18, the team describes assembling and successfully testing two of the three key components of a battery. A complete battery is on its way.

"To our knowledge, this is the first instance in which microcontact printing has been used to fabricate and position microbattery electrodes and the first use of virus-based assembly in such a process," wrote MIT professors Paula T. Hammond, Angela M. Belcher, Yet-Ming Chiang and colleagues. Read more in MIT Tech Talk.

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Tuesday, November 18, 2008

How to Merge Several FLARENET Models into Single Model ?

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Nowadays Oil & gas, LNG, Petrochemical, Refinery plant capacity are large and some time a few design centers are working together to manage the project during design phase. The project may splits into several large units and each design center will design their own units. The design include flare system modeling using FLARENET.

Several design center will generate their own FLARENET models and upto one point of time, all models may required to merge in order to check the overall flare system performance. Some steps presented in thmay be used to merge several FLARENET models into single model using built in utility in FLARENET.





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If you aware of any other method, please share with us.

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Monday, November 17, 2008

Tree Power

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A group of researchers with team member Andreas Mershin, a postdoctoral associate at the CBE and Christopher Love, an MIT senior in chemistry, led by Shuguang Zhang, the associate director of the MIT's Center for Biomedical Engineering (CBE) from the Massachusetts Institute of Technology (MIT) has managed to use the energy generated by trees to power a network of wireless sensors to prevent spreading forest fires. These sensors are powered by off-the-shelf batteries which is rechargeable by electricity generated by the trees.

Although the power generated by tree is small, it sufficient to produces enough electricity to enable four time signals emission a day from the system. This obviously a break through in power industrial where human being is still struggling with. It is believed the tree power may be adopted to be utilized in other wireless applications. Read more in "Using tree power to prevent forest fires?"

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Sunday, November 16, 2008

Check Valve Types and Selection

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Check valves or Non-return valves (NRV) are normally installed in piping to avoid back flow. Rotating equipment such as pump, compressor, etc will always be equipped with NRV(s) on the discharge to avoid back flow when rotating equipment is shut. Back flow creates severe surging to the rotating equipment and potentially damage the equipment. In certain process system, NRV will be employed to avoid contamination, overheating, etc due to back flow.

Check valves or Non-return valves (NRV) is basically an automatic valve open to allow forward flow and close to against reverse flow. In principle, it split into four basic types. There are swing, dual-plate, tilting disc and lifting type. Wrong selection of check valve type can leads to operability problem, leakage and continual maintenance issue.

Lift Check valves
- higher pressure drop is expected.
- equipped with small return spring to facilitate valve closure on reverse flow
- two type of seat. hard seat for for high differential pressure sealing and resilient seat for low differential pressure sealing
- shortest travel length. Fastest response.
- excellent performance for low and/or pulsating flows
- not good for fluid with particles
- Body install horizontal with disc / piston vertically
- Small check valve range from 1/2" to 2" lift piston type check valve
- Prefer operate in full open position

Minimum Recommended Line Velocity, Vmin (ft/s) = 12 SQRT (v)

where
v = Specific Volume of the Fluid (ft3/lb)




Lift Check Valve

Swing Check Valve
- Tight sealing / shut-off
- Low pressure drop
- Susceptible to water hammer
- Not good for low flow and/or pulsating flow
- Vertical (upward flow) & horizontal installation
- Easiest check valve to maintain
- Prefer operate in full open position

Swing check valves should be sized such that the flow velocity in the line is sufficient to hold the disc in the fully open position.

Minimum Recommended Line Velocity, Vmin (ft/s) = 75 SQRT(v)

where
v = Specific Volume of the Fluid (ft3/lb)



Swing Check Valve

Dual plate Check valve
The characteristic of dual plate check valve is pretty same as swing check valve.
- low pressure drop
- Not good for low flow and/or pulsating flow
- Vertical (upward flow) & horizontal installation
- Faster opening and closure compare to swing check valve
- Susceptible to water hammer (lesser than Swing check valve)
- Prefer operate in full open position


Dual Plate Check Valve

Tilting Disc Check Valves
- Fast opening and closing without damage to disc and seat
- Stable at low and pulsating flows
- Moderate pressure drop. Lower than lifting check valve but higher than swing check valve
- Vertical (upward) & horizontal installation
- Moderate tight sealing
- Prefer operate in full open position

Minimum Recommended Line Velocity, Vmin (ft/s) = 24 sqrt (v)

where
v = Specific Volume of the Fluid (ft3/lb)



Tilting Disc Check Valve


Selection Consideration
There are four (4) main criteria shall be considered for the selection of check valve type :
  • non-slam characteristic
  • pressure loss
  • cost
  • application
Comparative rating for each type of check valve have been provided for these criteria (specifically first two technical criteria). These rating will be plotted on a Check Valve Comparative Selection Chart and together budget for final selection. Read more in "Design and Selection of Check Valve".

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Friday, November 14, 2008

Mass Heat of Vaporization in HYSYS only for Pure Component

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Since the released of this article "Determine Latent Heat for Multi-Component and Relieving Area Using Rigorous Method in HYSYS", a few young engineers raised a question. The proposed method does not work for pure component i.e. pure propane. How shall i obtain the latent heat of pure component using HYSYS ?

The proposed method in "Determine Latent Heat for Multi-Component and Relieving Area Using Rigorous Method in HYSYS" is typically use to handle system with multi-component with large ranging of boiling point. It is typical useful for crude, naphtha, gasoline, condensate, etc. However, the propose method can not be used for pure component as it has only single boiling point at one pressure i.e. 152.4 Btu/lb at 100 psia for pure propane.



To obtain the latent heat of vaporization for pure component from HYSYS, it is pretty simple. From stream properties tab, latent heat of vaporization (Hvap) will be the Vapor Mass Enthalpy (Hv) minus Liquid Mass Enthalpy (Hl). Refer to above image. Hv = - 1032.6 Btu/lb, Hl = -1185 Btu/lb, thus Hvap = -1032.6 - (-1185) = 152.4 Btu/lb at 100 psia.



Another way is to read the Latent heat of Vaporization (Hvap) directly from properties tab. See above image. Mass Heat of Vap (Btu/lb) = 152.4 Btu/lb.

Important Note :
For pure component, latent heat of vaporization can be obtained by Vapor Mass Enthalpy (Hv) minus Liquid Mass Enthalpy (Hl).

For multi-component, latent heat of vaporization is NOT advisable to obtain by Vapor Mass Enthalpy (Hv) minus Liquid Mass Enthalpy (Hl). Rigorous method proposed in "Determine Latent Heat for Multi-Component and Relieving Area Using Rigorous Method in HYSYS" can be used.

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Thursday, November 13, 2008

Definition of Terms Related to PRESSURE

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A simple question always asked and debated by many engineers. What is the different between the following terms ?
  • Maximum Allowable Working Pressure (MAWP)
  • Design Pressure (PD)
  • Maximum Allowable Operating Pressure (MAOP)
  • Maximum Operating Pressure (PO,Max)
  • Normal Operating Pressure (PO)
  • Minimum Operating Pressure (PO,Min)
  • Minimum Allowable Operating Pressure (MinAOP)

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A mechanical engineer may have different understanding than a process engineer. A process engineer from an organization may have slightly different understanding than a process engineer from another organization. A process engineer educated and/or practising engineering in a country i.e China may have different interpretation than another process engineer educated and / or practising engineering in another country i.e. USA, UK, etc. This always creates a lot of confusion, unnecessary argument and rework. In worst event could lead to hazard. Thus, first far most important thing is to define correctly the meaning of each terms so that everyone have same understanding.

Following are the simple definition of above mentioned terms. Whenever a post contains one or more of these terms, the following shall be referred.

Normal Operating Pressure (PO) - System pressure as expected to be operated at during normal operation throughout the design life of the system.

Maximum Operating Pressure (PO, Max) - Maximum system pressure as expected during normal operation, may occur in some process transient period or different operating mode or campaigns and it built into the design to cater for any uncertainties due to start-up, fouled, decayed, etc. It provides some level of flexibility for a proper operation of the system throughout the entire life of the system.

Minimum Operating Pressure (PO, Min) - Minimum system pressure as expected during normal operation, may occur in some process transient period or different operating mode or campaigns and it built into the design to cater for any uncertainties due to start-up, fouled, decayed, etc. It provides some level of flexibility for a proper operation of the system throughout the entire life of the system.

Maximum Allowable Operating Pressure (MAOP) - Maximum system pressure that can be allowed to ensure a proper operation of an a device or system.

Minimum Allowable Operating Pressure (MinAOP) - Minimum system pressure that can be allowed to ensure a proper operation of an a device or system.

Design Pressure (PD) - A pressure chosen / specified (normally chosen by process engineer) to have certain margin (i.e. 10%) above the PO,Max (or MAOP). It is a maximum pressure in the system that :

- is NOT expected during normal operation
- may only occur during emergency situation such as fire, loss of utilities, valve failure, any abnormal operation corresponding to a short duration, mal-operation, etc

Design pressure becomes MINIMUM pressure that can be hold by any components within the system without mechanical failure. It is used to define the minimum MAWP of components within the system. For example, design pressure is used to calculate minimum vessel wall thickness.

Maximum Allowable Working Pressure (MAWP) - A maximum gauge pressure permissible by a equipment / device (at coincident temperature specified for that pressure) and is governed by code i.e. ASME, JIS, GB, etc

In many cases...

MinAOP <= PO,Min <= PO <= PO,Max < MAOP < PD <= MAWP

Example :
A pressure vessel contains instrument air is normally operate between 6 - 8 barg. The system would trip under Low-Low pressure of 5 barg to allow sufficient instrument air volume for safe operation of some critical valve during shutdown. The system is designed for 11 barg as specified by the process designer. A conventional spring loaded pressure relief valve (PRV) is provided to protect the vessel from overpressure. The minimum wall thickness required for 11 barg is 6.27 mm, plus 1.5 mm corrosion allowance as specified by process engineer, the total required wall thickness is 7.77 mm. Mechanical engineer has decided to provide 8.0 mm as wall thickness which correspondence to 12 barg.

(Note : all parameters have been selected arbitrary. Just for illustration only.)
  • Maximum Allowable Working Pressure (MAWP) = 12 barg
  • Design Pressure (PD) = 11 barg
  • Maximum Allowable Operating Pressure (MAOP) = 10 barg (~90% of 11 barg)
  • Maximum Operating Pressure (PO,Max) = 8 barg
  • Normal Operating Pressure (PO) = 7 barg
  • Minimum Operating Pressure (PO,Min) = 6 barg
  • Minimum Allowable Operating Pressure (MinAOP) = 5 barg
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Wednesday, November 12, 2008

Chemical Engineering Digital Issue for November 2008

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FREE Chemical Engineering Digital Issue for November 2008 has just been released !
Chemical Engineering magazine has just released November 2008 issue. If you are the subscriber of Chemical Engineering, you shall received similar notification.

Interesting articles
for this month:

2008 Salary Report Ch.E.s
Wonder when the CPI will feel the hit of the weakening world economy

Process Modeling Moves Center-Stage
A model solution for the CPI: Reducing risk while increasing profit

When Size Matters
Particle sizing equipment gets updated to meet the changing needs of the CPI

Biodiesel Production
This one-page guide illustrates the process of biodiesel production by basecatalyzed transesterification of vegetable oil

Condition-Based Maintenance Management Enhances Reliability
Understand reliability, condition monitoring and maintenance management to keep rotating equipment in top form

Get More From Vertical Thermosiphon Reboilers
The effects of three different heat-transfer-enhancement devices are outlined here

Temperature and Pressure Measurement
Calibrate high-quality thermometers with this instrument; A pressure transducer for hazardous applications is introduced; Ultra-compact pressure transmitters offer

If you yet to be subscriber of Chemical Engineering, requested your FREE subscription via this link (click HERE). Prior to fill-up the form, read "Tips on Succession in FREE Subscription".

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