- •G. Zayonchkovsky, V. Stadnychenko, y. Golovko «hydraulic machines and hydraulic/pneumatics equipment»
- •Introduction
- •Pump glossary
- •1.2 Pump history
- •1.3 Pump family group
- •1.3.1 Centrifugal pumps
- •1.3.2 Reciprocating pumps
- •1.3.3 Pump selection
- •2.1 Centrifugal pumps
- •2.2 Centrifugal pump characteristics
- •2.3 Performance modifications for varying pipelene applications
- •2.3.1 Cavitation
- •2.3.2 Net positive head
- •2.3.3 Net Positive Suction Head Avaible
- •2.3.4 Net Positive Suction Head Required
- •2.3.5 Correcting for Inadequate Suction Conditions
- •2.3.6 Npsha-nphsr Criteria
- •2.3.7 Viscous Liquids
- •2.3.8 Minimum Flow
- •2.3.9 Temperature Rise
- •2.3.11 Centrifugal Pump Station Piping Design
- •2.3.12 Centrifugal Pump Nozzle Loading
- •2.3.12 Pump Operational Hazards and Risk
- •3.1. Rotary
- •3.2 Types of rotary pumps
- •3.3 Reciprocating pumps
- •3.4 Piston pumps
- •4.1 Role of compression in a gas pipeline network
- •4.2 Gas pipeline hydraulics principles
- •4.3 Friction factor
- •4.4 Flow regimen profiles calculation
- •4.4 Pipeline design and optimization
- •4.4.1 Optimization Parameters
- •Optimization Process Overview
- •4.4.3 Selection of Alternative
- •4.4.4 Sensitivity Analysis
- •4.4.5 Pipeline Looping & Compression (Location & Spacing)
- •Hydraulics Simulations
- •4.4.7 Compressor Operation Costs
- •5.1. Pneumatic piping, hoses and connections
- •5.2 Flow control and pressure regulation valves
- •5.3 Relief valves dynamics
- •6.1 Linear actuators
- •6.2 Construction
- •6.3 Mounting arrangements an cylinder dynamics
- •7.1 Station piping layout
- •7.2 Scrubbers and filters
- •7.2.1 Dry scrubbers
- •7.2.1 Wet scrubbers
- •Categorization of wet scrubbers
- •Advantages and disadvantages
- •7.2.3 Filters
- •7.3 Gas coolers
- •7.4 Absorbers and regenerators
7.2.1 Wet scrubbers
Wet scrubber is a form of pollution control technology. The term describes a variety of devices that remove pollutants from a furnace flue gas or from other gas streams. In a wet scrubber, the polluted gas stream is brought into contact with the scrubbing liquid, by spraying it with the liquid, by forcing it through a pool of liquid, or by some other contact method, so as to remove the pollutants.
The design of wet scrubbers or any air pollution control device depends on the industrial process conditions and the nature of the air pollutants involved. Inlet gas characteristics and dust properties (if particles are present) are of primary importance. Scrubbers can be designed to collect particulate matter and/or gaseous pollutants. Wet scrubbers remove dust particles by capturing them in liquid droplets. Wet scrubbers remove pollutant gases by dissolving or absorbing them into the liquid.
Any droplets that are in the scrubber inlet gas must be separated from the outlet gas stream by means of another device referred to as a mist eliminator or entrainment separator (these terms are interchangeable). Also, the resultant scrubbing liquid must be treated prior to any ultimate discharge or being reused in the plant.
|
|
Figure 7-3. Wet scrubber. a -Venturi scrubber with mist eliminator, b - Packed bed tower |
|
There are numerous configurations of scrubbers and scrubbing systems, all designed to provide good contact between the liquid and polluted gas stream. Figures 7-3a and 7-3b show two examples of wet scrubber designs, including their mist eliminators. Figures 7-3a is a venturi scrubber design. The mist eliminator for a venturi scrubber is often a separate device called a cyclonic separator. Figures 7-3b has a tower design where the mist eliminator is built into the top of the structure. Various tower designs exist.
A wet scrubber's ability to collect small particles is often directly proportional to the power input into the scrubber. Low energy devices such as spray towers are used to collect particles larger than 5 micrometers. To obtain high efficiency removal of 1 micrometer (or less) particles generally requires high energy devices such as venturi scrubbers or augmented devices such as condensation scrubbers. Additionally, a properly designed and operated entrainment separator or mist eliminator is important to achieve high removal efficiencies. The greater the number of liquid droplets that are not captured by the mist eliminator the higher the potential emission levels.
If the gas stream contains both particle matter and gases, wet scrubbers are generally the only single air pollution control device that can remove both pollutants. Wet scrubbers can achieve high removal efficiencies for either particles or gases and, in some instances, can achieve a high removal efficiency for both pollutants in the same system. However, in many cases, the best operating conditions for particles collection are the poorest for gas removal.
In general, obtaining high simultaneous gas and particulate removal efficiencies requires that one of them be easily collected (i.e., that the gases are very soluble in the liquid or that the particles are large and readily captured) or by the use of a scrubbing reagent such as lime or sodium hydroxide.
Typical wet scrubbing process can be described as follows:
Hot flue gas from a furnace enters a saturator (if present) where gases are cooled and humidified prior to entering the scrubbing area. The saturator removes a small percentage of the particulate matter present in the flue gas.
Next, the gas enters a venturi scrubber where approximately half of the gases are removed. Venturi scrubbers have a minimum particle removal efficiency of 95%.
The gas flows through a second scrubber, a packed bed absorber, where the rest of the gases (and particulate matter) are collected.
An entrainment separator or mist eliminator removes any liquid droplets that may have become entrained in the flue gas.
A recirculation pump moves some of the spent scrubbing liquid back to the venturi scrubber where it is recycled and the remainder is sent to a treatment system.
Treated scrubbing liquid is recycled back to the saturator and the packed bed absorber.
Fans and ductwork move the flue gas stream through the system and eventually out the stack.
