Asus G71Gx ENE CIR Driver
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Asus G71Gx ENE CIR Driver
As discussed in the August 18, final rule listing as hazardous the coking wastes covered by this background document, this exclusion applies to KK, K, and K14S waste streams when they are recycled, as specified.
K, and K wastes by establishing BOAT treatment standards numerically equivalent to the universal treatment standards universal standards. A universal standard is a single concentration limit established for a specific constituent regardless of the waste raatru in which it is present i. These two sets Asus G71Gx ENE CIR in he population of regulated constituents and in the individual universal standards.
Volume B: Universal Standard Wastes Table presents the BOAT treatment standards for wastewater forms of these wastes. The standards shown on Tables and are Asus G71Gx ENE CIR equivalent to the universal standards for those constituents. Section 3. Existing waste management practices for these wastes also are described in Section 3 0.
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Section 4 0 explains the Asus G71Gx ENE CIR and rationale for selection of the regulated constituents, discusses the treatment technologies the Agency has designated as "applicable" and "demonstrated" for these wastes, Asus G71Gx ENE CIR BDAT for wastewater and nonwastewater forms of these wastes, and presents the determination of the BDAT treatment standards for these wastes. Acknowlcdgcmeo'j are provided in Sect,on 70 Tables are located at the end of each Asus G71Gx ENE CIR.
NR - Not Regulated. T rf k. The Agency performed an extensive study of the coke by-products industry and made the determination, based on the evaluation presented in the Listing Background Document for Coking Wastes referred to as the Listing Background Document 1,2 and pursuant to the HSWA mandate, to list as hazardous the following seven wastes associated with the production.
The information that supports these findings is presented in the Listing Background Document, and in the RCRA Docket supporting the listing of coking wastes The coking wastes listed as KK14S, K, and K which are more fully described in Section 3 0 include both process residues and storage tank residues. According to the infnrmaiion available to the Agency, all units in which these wasteuaters are managed are er. The Agency did not believe that any tar refining facility is land disposing wastewaters.
Thus, the Agency concluded that no additional environmental benefit uouJd be derived from listing these wastewaters as hazardous. Many of the coke by-products residues listed as hazardous wastes are recycled by a substantial segment of the industry.
Two recycling techniques are Asus G71Gx ENE CIR as commonly used: The coke by-products recovery industry includes both captive and merchant facilities. Iron and steelmaking facilities own captive facilities and use nearly all their produced coke in the production of steel 1. Merchant coke facilities generally produce blast furnace Asus G71Gx ENE CIR for sale to iron and steel companies, and metallurgical coke for sale to iron and steel foundries and other chemical facilities 2.
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The coke is removed from the Asus G71Gx ENE CIR oven and sold as product The coke oven gas exits the coke oven through the collecting main where it is sprayed with flushing liquor. The flushing liquor primarily contains water, tar, light oils, and heavy hydrocarbons.
The flushing liquor cools the coke oven gas, causing precipitation of tar and condensation of nonvolatde organics from the gas. The flushing liquor carries coal tar, Asus G71Gx ENE CIR, and ammonia to the tar decanter tank 1 In the tar decanter tank, the material separates into three layers- the top layer is flushing liquor, the middle layer is coal tar, and the bottom layer contains carbonaceous deposits which were entrained in the Asus G71Gx ENE CIR and Liquor in the collecting main 2.
A portion of the flushing liquor is recycled to the collecting main or to the primary cooler.
The remaining portion, Asus G71Gx ENE CIR referred to as excess ammonia liquor, is routed to the excess ammonia liquor tank, phenol extraction used for sodium pbenolate recoveryand the ammonia stills used for ammonia recovery. The waste ammonia liquor from the ammonia stills is routed to the wastewater treatment system. Tar is drained from the middle layer, routed to tar dcwatering where it is dewatcred by gravity separation, and collected in tar storage tanks.
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Over time a tar residue K wastes at coke by-products recovery facilities or K wastes at tar refining facilities accumulates at the bottom of the tar storage tanks and reportedly must be removed to maintain storage Asus G71Gx ENE CIR 1,2. Wastewater from tar dewatenng is discharged to the wastewater treatment system.
The uncondensed coke oven gas flows from the collecting main to the suction main, and enters the primary cooler. As the gas temperature is reduced in the primary cooler, additional tar and liquor condense.
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The coke oven gas that exits the primary cooler is compressed in an exhauster and conveyed to an electrostatic prec. Once removed, this coal tar is often rojted to the tar collecting sump 1,2.
Coke by-products recovery facilities often recover ammonia from coke oven gas and excess ammonia liquor 1,2 Ammonia is recovered from the gas stream by either the direct recovery Asus G71Gx ENE CIR, involving contact of the entire gas stream with?. The ammonium sulfate crystals from the direct process undergo drying. Condensed water from the dryer is discharged to the uastcua: When using water in the final cooler, naphthalene in the coke oven gas condenses and is removed from the cooling water.
The effluent stream from the final cooler is sent to Asus G71Gx ENE CIR naphthalene separator, where naphthalene is skimmed from the water surface.