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Vapor treatment

Vapor Treatment. The vapors from the tank space can be sent to a treatment system (condenser, absorption, etc.) before venting. The system shown in Fig. 9.1 uses a vacuum-pressure relief valve which allows air in from the atmosphere when the liquid level falls (Fig. 9.1a) but forces the vapor through a treatment system when the tank is filled (Fig. 9.16). If inert gas blanketing is required, because of the flammable nature of the material, then a similar system can be adopted which draws inert gas rather than air when the liquid level falls. [Pg.260]

Figure 9.1 Storage tank fitted with a vapor treatment system. (From Smith and Petela, The Chemical Engineer, no. 517, 9 April, 1992 reproduced by permission of the Institution of Chemical Engineers.)... Figure 9.1 Storage tank fitted with a vapor treatment system. (From Smith and Petela, The Chemical Engineer, no. 517, 9 April, 1992 reproduced by permission of the Institution of Chemical Engineers.)...
Fig. 2 Fluorescence plots of the sugars after separation on a Si-50 000 layer without ammonia-vapor treatment. Start (1), raffinose (2), lactose (3), sucrose (4), glucose (5), fructose (6). Fig. 2 Fluorescence plots of the sugars after separation on a Si-50 000 layer without ammonia-vapor treatment. Start (1), raffinose (2), lactose (3), sucrose (4), glucose (5), fructose (6).
Fig. 1 Chromatogram of fatty oils (9 pg each per 10 mm band) after iodine vapor treatment (A) and after additional immersion in a starch solution (B) Itack 1 avocado oil, Hack 2 sunflower oil, Tlack 3 linseed oil, Tlack 4 almond oil. Fig. 1 Chromatogram of fatty oils (9 pg each per 10 mm band) after iodine vapor treatment (A) and after additional immersion in a starch solution (B) Itack 1 avocado oil, Hack 2 sunflower oil, Tlack 3 linseed oil, Tlack 4 almond oil.
The type of vapor treatment that is used will depend on factors such as the contaminant concentrations in the extracted vapors and the air emission discharge limitations for the site. Highly contaminated vapors at a site with stringent air emission limitations may require a multistep vapor treatment train, such as thermal oxidation, followed by carbon adsorption. Less contaminated vapors at a site with less stringent air emission limitation may require minimal or no vapor treatment. Fields et al.38 described the following rules of thumb for selecting vapor treatment ... [Pg.1008]

Kato, K. 1998. Low-temperature synthesis of SrBi2Ta209 ferroelectric thin films through the complex alkoxide method Effects of functional group, hydrolysis and water vapor treatment. Jpn. J. Appl. Phys. 37 5178-5184. [Pg.70]

Well spacing/flow requirements Compressor size Blower size/well placement Vapor treatment... [Pg.276]

Assess extent of impacted soil Excavate, crush, aerate, and replace Maintain documentation Confirm effectiveness Requires vapor treatment circumstances ... [Pg.295]

A pilot soil vapor extraction test was performed to determine whether this method would be effective to mitigate the concern. Such a test provided information used to design a full-scale recovery and vapor treatment system. With air permeabilities on the order of 1 to 3 D and TPH vapor concentration on the order of 330 ppm (weight), the pilot test supported SVE as a viable remediation approach. [Pg.319]

Vapor treatment equipment consisting of two serial filters containing 1000 lb of granulated activated charcoal (GAC) situated upstream of the SVE blower and... [Pg.319]

LNAPL recovery projects require careful planning, operation, and management. Some additional factors become important at unforeseen times. Recovery of free product often produces flammable vapors at concentrations that can violate air quality standards if freely released. Vapor treatment should be considered early in the design process. Storage of flammable liquids in appropriate containers is necessary. [Pg.342]

For another site in Regina in 1995, a total cost for 11 fractured wells, two soil vapor extraction systems, and operation and maintenance for 6 months was approximately 80,000. This figure did not include vapor treatment since none was required. Colder estimated that, had hydraulic... [Pg.667]

According to the vendor, the cost of DNAPL vaporization is 15 to 45/yd, excluding vapor treatment (D168596). [Pg.1030]

TerraTherm Environmental Services, Inc., a subsidiary of Shell Technology Ventures, Inc., has developed the in situ thermal desorption (ISTD) thermal blanket technology to treat or remove volatile and semivolatile contaminants from near-surface soils and pavements. The contaminant removal is accomplished by heating the soil in sim (without excavation) to desorb and treat contaminants. In addition to evaporation and volatilization, contaminants are removed by several mechanisms, including steam distillation, pyrolysis, oxidation, and other chemical reactions. Vaporized contaminants are drawn to the surface by vacuum, collected beneath an impermeable sheet, and routed to a vapor treatment system where contaminants are thermally oxidized or adsorbed. [Pg.1042]

Vapors released by heating are drawn to the surface by vacuum extraction and routed to a vapor treatment system where they are destroyed in a flameless thermal oxidizer. According to the vendor, thermal wells can remediate contamination at depths previously thought to be unreachable and/or untreatable. [Pg.1043]

The Thermatrix, Inc., PADRE process is a commercial, off-gas treatment technology that purifies airstreams contaminated with volatile organic compounds (VOCs). The PADRE vapor treatment process traps VOCs using filter beds that contain a proprietary resin. This regenerative adsorption method involves an on-line treatment bed for infiuent air, while another bed undergoes a desorption cycle. PADRE often works in conjunction with soil vapor extraction or air stripping systems. The PADRE process can be applied at site remediation projects, industrial wastewater facilities, and industrial air processing sites. [Pg.1055]

Estimated unit prices for treatment of VOCs using the PADRE vapor treatment process range between 1.00 and 3.00/lb. The initial contaminant concentration, volume of gas stream to be treated, and target cleanup levels have signihcant impact on unit price. These price estimates do not necessarily include all indirect costs associated with treatment, such as excavation, permits, and treatment of residuals (D13375F, p. 15). [Pg.1056]

Eliminates the need for surface water treatment may eliminate the need for surface vapor treatment for aerobically biodegradable contaminants in permeable soils. [Pg.1115]


See other pages where Vapor treatment is mentioned: [Pg.261]    [Pg.405]    [Pg.976]    [Pg.1008]    [Pg.1011]    [Pg.1013]    [Pg.1035]    [Pg.627]    [Pg.160]    [Pg.371]    [Pg.630]    [Pg.664]    [Pg.815]    [Pg.1055]    [Pg.1112]    [Pg.209]    [Pg.212]    [Pg.217]    [Pg.448]    [Pg.448]    [Pg.405]    [Pg.360]    [Pg.2]    [Pg.5]    [Pg.8]    [Pg.10]   
See also in sourсe #XX -- [ Pg.139 ]

See also in sourсe #XX -- [ Pg.14 , Pg.17 ]




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