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		<id>https://wiki.rpg.net/index.php?title=Bag_filter&amp;diff=135162</id>
		<title>Bag filter</title>
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		<updated>2010-01-18T02:33:46Z</updated>

		<summary type="html">&lt;p&gt;114.91.237.190: Created page with &amp;#039;== Bag Filter ==  WHAT IS BAG FILTER?  Recovery of particulate matter from exhaust gas is vital for any industry from two aspects  To avoid pollution problems  Recovery of finish…&amp;#039;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;== Bag Filter ==&lt;br /&gt;
&lt;br /&gt;
WHAT IS BAG FILTER?&lt;br /&gt;
&lt;br /&gt;
Recovery of particulate matter from exhaust gas is vital for any industry from two aspects&lt;br /&gt;
&lt;br /&gt;
To avoid pollution problems &lt;br /&gt;
Recovery of finished product-increasing the plant yield &lt;br /&gt;
For recovering particulate matter different options available are – Cyclones, Venturi, scrubbers, bag filters, electrostatic precipitators etc. Out of these bag filter becomes the best choice if following are dominant selection criteria’s:&lt;br /&gt;
&lt;br /&gt;
Material is expensive and hence high collection efficiency is desired. &lt;br /&gt;
Particulate size is very fine. &lt;br /&gt;
Material recovery in powder form is desirable &amp;amp; not in solution form. &lt;br /&gt;
A conventional bag filter normally has following problems:&lt;br /&gt;
&lt;br /&gt;
Frequent bag choking - hence high plant shut down time. &lt;br /&gt;
Higher pressure drops across bag filter – hence higher blower electrical power. &lt;br /&gt;
Bag choking resulting in reduced airflow rate &amp;amp; therefore reduction in plant capacity. &lt;br /&gt;
Due to the above the bag filter becomes bottleneck for plant operation. &lt;br /&gt;
&lt;br /&gt;
Realizing above we have designed our bag filter using scientific procedure as elaborated in DESIGN METHODOLOGY. We manufacture bag filter as per &amp;quot;Quality Assurance Plan.&amp;quot; Hence consistency in quality is guaranteed. &lt;br /&gt;
 &lt;br /&gt;
  &lt;br /&gt;
&lt;br /&gt;
WORKING PRINCIPLE OF BAG FILTER&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Figure 1 depicts the working principle of bag filter.&lt;br /&gt;
&lt;br /&gt;
See Figure No.1&lt;br /&gt;
&lt;br /&gt;
The dust-laden air enters the bag filter bustle. &lt;br /&gt;
The air is uniformly distributed avoiding channeling. &lt;br /&gt;
Initially a coat of material forms on the bags. Subsequently, the coat acts as the filtering medium. &lt;br /&gt;
The dust is accumulated on filter elements while the air passes thorough the filter bags from outside to inside. &lt;br /&gt;
The accumulated powder is dislodged from the bags by reverse pulse-jet air intermittently. &lt;br /&gt;
The dislodged powder falls on bottom cone and is discharged through powder discharge valves. &lt;br /&gt;
The dust free air is sucked by induced draft fan and is exhausted to atmosphere. &lt;br /&gt;
Knockers are provided on conical portion especially for sticky/hygroscopic materials. &lt;br /&gt;
 &lt;br /&gt;
 &lt;br /&gt;
&lt;br /&gt;
MAIN COMPONENTS OF BAG FILTER&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
Bag filter housing &lt;br /&gt;
Filter bags &lt;br /&gt;
Bag cages &lt;br /&gt;
Filter bag–Venturi assembly &lt;br /&gt;
Pulse-jet air cleaning assembly &lt;br /&gt;
Air bleeding assembly &lt;br /&gt;
1. Bag filter housing:&lt;br /&gt;
&lt;br /&gt;
Bigger housing size is required for sufficient filtering area and low CAN velocity. It ensures minimum pressure drop across bag filter. This reduces the blower power consumption. &lt;br /&gt;
Bustle type construction at air inlet assures uniform air distribution. This avoids channeling of air and hence gives consistent bag filter performance. &lt;br /&gt;
Bottom cone angle of bag house cone is 45?so that the powder slides freely. &lt;br /&gt;
Higher area is provided for air passage to keep the CAN VELOCITY low. This avoids powder &amp;quot;re-entrainment&amp;quot; and resultant bag choking. &lt;br /&gt;
Full SS construction is provided even on exhaust side - longer bag filter life. &lt;br /&gt;
Bag removal from top - maintenance in dust free atmosphere. &lt;br /&gt;
Figure 2 explains these points.&lt;br /&gt;
&lt;br /&gt;
See Figure No.2&lt;br /&gt;
&lt;br /&gt;
 2. Filter bags:&lt;br /&gt;
&lt;br /&gt;
We careful select filter bag fabric considering temperature, particulate size, air-to- cloth ratio. &lt;br /&gt;
The Felt media bag minimizes pressure fluctuations giving uniform and high collection efficiency. &lt;br /&gt;
Specially selected Anti-stick coating on bags minimizes bag choking. &lt;br /&gt;
3. Bag cages&lt;br /&gt;
&lt;br /&gt;
Figure 3 shows our cage construction.&lt;br /&gt;
&lt;br /&gt;
See Figure No.3&lt;br /&gt;
&lt;br /&gt;
Cages are made out of larger diameter bars to make the assembly rigid.&lt;br /&gt;
&lt;br /&gt;
The pitch between bars is kept less to adequately support bags by cages. This avoids flex line failure between the vertical wires. &lt;br /&gt;
Careful selection of fit relationship between cage and bag avoid premature bag failure. &lt;br /&gt;
If bag is oversized then bags may have internal abrasion along vertical lines causing bag failure. &lt;br /&gt;
Sharp edges on Pan are avoided as they cut / damage the bag where it comes in contact with the edge of Pan. &lt;br /&gt;
4. Filter bag-Venturi assembly&lt;br /&gt;
&lt;br /&gt;
Figure 4 explains our Venturi assembly.&lt;br /&gt;
&lt;br /&gt;
See Figure No.4&lt;br /&gt;
&lt;br /&gt;
Higher thickness Venturi mounting plate – uniform pressure is applied - seals better. &lt;br /&gt;
Venturi are cast –rigidity in clamping reducing leakages. &lt;br /&gt;
Special Silicone gasket ensures Leak-proof joint between Venturi and Venturi mounting plate. &lt;br /&gt;
Clamps are provided to hold the bags on cages and seal for leakages. &lt;br /&gt;
5. Reverse PulseJet cleaning system&lt;br /&gt;
&lt;br /&gt;
Figure 5 explains working of reverse jet system.&lt;br /&gt;
&lt;br /&gt;
See Figure No.5&lt;br /&gt;
&lt;br /&gt;
6. Air bleeding arrangement&lt;br /&gt;
&lt;br /&gt;
A temperature monitored automatic &amp;quot; Air bleeding ’’ arrangement avoids exposure of bags to higher temperatures and ensures longer bag life. &lt;br /&gt;
Figure 6 explains the construction.&lt;br /&gt;
&lt;br /&gt;
See Figure No.6&lt;br /&gt;
 &lt;br /&gt;
  &lt;br /&gt;
&lt;br /&gt;
DESIGN METHODOLOGY&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
In our every Bag filter design following scientific procedure is adopted.&lt;br /&gt;
&lt;br /&gt;
For calculating filtering area selection of filtering velocity is done from reference tables based on material properties. &lt;br /&gt;
This filtering velocity needs to be corrected to suit the actual operating conditions. Following four factors are considered: &lt;br /&gt;
1. Application Factor: It varies for oily, moist, agglomerating material and depending on     continuous/intermittent operation. e. g. 0.9 for heavy dust loads and continuous operation.&lt;br /&gt;
&lt;br /&gt;
2. Temperature Factor: It varies as per gas stream temperature. e. g. 1.0 for temperatures  upto 45 deg.&lt;br /&gt;
&lt;br /&gt;
3. Particle size factor: It depends on particle size. e. g. 0.8 for below 3 micron.&lt;br /&gt;
&lt;br /&gt;
4. Dust load factor: It varies as per dust loading per volume of gas stream. &lt;br /&gt;
&lt;br /&gt;
e. g. 1.2 for 10 or less grains/cu.ft.&lt;br /&gt;
&lt;br /&gt;
In addition to the filtration velocity, consideration of &amp;quot;CAN VELOCITY&amp;quot; is critical while sizing bag filter. CAN VELOCITY is the velocity in the flow passages between the filter bags. &lt;br /&gt;
With high CAN VELOCITY, the dust particles, which have been cleaned off the bags, get RE-ENTRAINED in the gas stream. This re-entrained dust gets RE-DEPOSITED on bags. This results in higher pressure drop and consequential deterioration in bag filter performance. Following fig. Shows this effect. &lt;br /&gt;
The CAN VELOCITY is selected based on the material, bag length. This decides the bag filter house sizing. &lt;br /&gt;
 &lt;br /&gt;
  &lt;br /&gt;
&lt;br /&gt;
EXCLUSIVE FEATURES OF BAG FILTER&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
 Better performance -  &lt;br /&gt;
&lt;br /&gt;
The pressure drop across [http://www.boocca.com/en/bag-filter/ bag filter] is very low (40 - 100 mm WC) even for continuous operation. This results in reduced power consumption of fan. &lt;br /&gt;
Movement of air from top to bottom aids in removing powder from bags eliminating the possibilities of dust re-entrainment. This results in low-pressure drop and precious energy saving. &lt;br /&gt;
Anti-stick coat on bags facilitates removal of powder avoiding chocking of filter bags. &lt;br /&gt;
Automatic air pulse jet system with adjustable sequential timer to clean filter bags on-line. &lt;br /&gt;
Bottom cone angle of housing is 450 hence powder slides freely down. &lt;br /&gt;
 Ease in maintenance and long life -  &lt;br /&gt;
&lt;br /&gt;
Bag removal from top facilitates maintenance in dust free atmosphere. &lt;br /&gt;
The bag cage has 16 wire rods for better support to bag that improve bag life. &lt;br /&gt;
Aluminum di-cast heavy wall thickness machined venturies for distortion free and leak free performance. Heavy wall thickness renders long life. &lt;br /&gt;
 Safety Instrumentation and Alarm -  &lt;br /&gt;
&lt;br /&gt;
Fully automatic temperature controlled Cold Air Bleeding system to limit air inlet temperature to protect the filter bag fabric. &lt;br /&gt;
Differential pressure switch across bag filter is provided to know if bags are chocked. &lt;br /&gt;
Vacuum pressure switch is provided to protect the housing and bags from collapsing under vacuum. &lt;br /&gt;
Compressed air pressure switch is provided on pulse jet cleaning system to ensure sufficient pressure is available for proper cleaning of filter bags online. &lt;br /&gt;
 The bag filter is compact. This results in low civil and erection cost.&lt;/div&gt;</summary>
		<author><name>114.91.237.190</name></author>
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