Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Energy recovery systems

For the same production capacity, the oxygen-based process requires fewer reactors, all of which operate in parallel and are exposed to reaction gas of the same composition. However, the use of purge reactors in series for an air-based process in conjunction with the associated energy recovery system increases the overall complexity of the unit. Given the same degree of automation, the operation of an oxygen-based unit is simpler and easier if the air-separation plant is outside the battery limits of the ethylene oxide process (97). [Pg.460]

Determination of Energy Output and Ejflciency for Energy-Recovery Systems An analysis of the amount of energy produced... [Pg.2246]

FIG. 25-65 Flow sheet—alternative energy recovery systems. [Pg.2248]

There is an important feedback factor which cannot be properly evaluated at this time. It concerns future municipal investment in a specific waste control system. This could result in legislation controlling the input of important potential waste materials to the municipality. For example large capital investment in a heat/energy recovery system based on incineration might induce legislative restrictions on low calorific materials like metals and glass. [Pg.104]

The goal of these systems is to use as much as possible of the thermal energy that is available above the ambient temperature. They are calleddirect energy-recovery systems. They do two things they reduce the amount of energy that must be supplied and also reduce the amount of cooling water that is necessary. This, in turn, can also decrease the amount of thermal pollution. [Pg.182]

The zero-emission energy recycling system (ZEROS) is a closed-loop thermal oxidation process that incinerates waste and recycles flue gas emissions for electrical co-generation. The technology uses a two-stage plasma torch combustion system, energy recovery system, and combustion gas cleanup systems. [Pg.1147]

The energy recovery system selected dictates the extent that solid waste must be prepared. Some systems require nothing more than the removal of massive noncombustibles, such as kitchen appliances from the refuse, while other processes require extensive shredding, air classification, reshredding, and drying, In conjunction with fuel preparation, it is usually worthwhile to reclaim metals and glass for recycling. [Pg.1717]

Some energy recovery systems require drying to remove excess moisture in the waste. This is required when sewage sludge is used as a fuel. Usually, waste heat from the total process can be used for the drying system. [Pg.1717]

The permeate of the MF units is fed to two SWRO units equipped with high-pressure pumps with an energy-recovery system (Pelton wheel). The SWRO units comprise 44 pressure vessels loaded with 6 Dow/FilmTec SW30 membranes each. The designed permeate capacity of each unit is 210 m3/h per unit with a recovery of 50-5 5%. Antisealant is dosed to the feed stream of the SWRO with a concentration of 3 to 4 ppm [15]. [Pg.270]

Shah, J.V. and Westerberg, A.W., "EROS—A Program for Quick Evaluation of Energy Recovery Systems," to appear, Computers and Chem. Eng., 1979. [Pg.91]

Energy consumption of 9-11 kWh/kg A1 Anode-cathode distance of 1-2 cm Energy recovery systems... [Pg.520]

Fig. 24.7. Schematic of acid heat to steam energy recovery system, after Puricelli et al., 1998. It is for intermediate H2S04 making, Fig. 9.6. Note (i) the double packed bed H2S04 making tower and (ii) boiler. Industrial acid heat recovery H2S04 making towers are 25m high and 10 m diameter. They produce 2000 to 4000 tonnes of H2S04 per day. For photographs see Sulfur, 2004.--------- large flows. small flows. Fig. 24.7. Schematic of acid heat to steam energy recovery system, after Puricelli et al., 1998. It is for intermediate H2S04 making, Fig. 9.6. Note (i) the double packed bed H2S04 making tower and (ii) boiler. Industrial acid heat recovery H2S04 making towers are 25m high and 10 m diameter. They produce 2000 to 4000 tonnes of H2S04 per day. For photographs see Sulfur, 2004.--------- large flows. small flows.
Alloys currently used in heat-from-acid energy recovery systems are ... [Pg.283]

Acid plants (especially sulfur burning plants) are now often built with acid heat to steam energy recovery systems. These significantly increase acidmaking energy efficiency. [Pg.284]

Energy consumption for manufacture of demineralized water from seawater is an issue, which has received much attention. Criscuoli and Drioli [132] found the energy costs for RO to be between 4 and 12 kW h m depending on whether or not an efficient energy recovery system was in place. Cabassud and Wirth [133] have estimated costs for VMD using PVDF hollow fiber membranes for salt concentrations varying between 15 and 300 g L (Table 19.3). [Pg.540]

Thermal. Combustion techniques bum waste for the recovery of heat energy, Waterwall combustors are the most technically developed energy recovery systems and employ special grates to bum "as received urban waste and recover steam either at saturated or superheated conditions. Over 250 plants are operating worldwide seven of them in the United States. Three of the seven were originally built as incinerators. Worldwide there have been a number of technical problems, with the control of corrosion and erosion being the most serious. The most recent European designs have solved these problems but at an increased capital cost. [Pg.17]

In the U.S., we have tried to develop new advanced chemical systems while the remainder of the world has continued to build mass burning energy recovery systems. [Pg.67]

Fischer, J.C. Optimizing lAQ, humidity control, and energy efficiency in school environments through the application of desiccant-based total energy recovery systems. lAQ 96 Paths to Better Building Environments. ASHRAE Atlanta, GA, 1996 179-194. [Pg.626]

Both the brackish and seawater reverse osmosis product water costs are based on 1982 costs and they are indicative of specific plants in an assumed location in the southern United States. The cost of energy in the seawater system assumes that the reject from the first stage high pressure reverse osmosis system is sent to an energy recovery system which reduces the overall energy requirements for the total system by 31%. [Pg.304]


See other pages where Energy recovery systems is mentioned: [Pg.52]    [Pg.2244]    [Pg.460]    [Pg.968]    [Pg.10]    [Pg.124]    [Pg.90]    [Pg.201]    [Pg.118]    [Pg.96]    [Pg.96]    [Pg.2000]    [Pg.1134]    [Pg.139]    [Pg.141]    [Pg.199]    [Pg.202]    [Pg.185]    [Pg.2489]    [Pg.2489]    [Pg.22]    [Pg.619]    [Pg.121]    [Pg.374]    [Pg.919]   
See also in sourсe #XX -- [ Pg.76 , Pg.77 , Pg.78 ]




SEARCH



Recovery system

© 2024 chempedia.info