BF flotation cell has two types: type I and type II. Type I is improved as suction cell referring to model SF; type II is improved as direct flow cell referring to model JJF.
Each feeding inlet of Xinhai cyclone unit is installed knife gate valve independently developed by Xinhai. This valve with small dimension reduces the diameter of cyclone unit.
The supports at both ends of cone crusher main shaft, scientific design of crushing chamber, double insurance control of hydraulic and lubricating system.
Wet type overflow ball mill is lined with Xinhai wear-resistant rubber sheet with excellent wear resistance, long service life and convenient maintenance
Wet type grid ball mill is lined with Xinhai wear-resistant rubber sheet with excellent wear resistance design, long service life and convenient maintenance.
Ring groove rivets connection, plate type screen box, advanced structure, strong and durable Vibration exciter with eccentric shaft and eccentric block, high screening efficiency, large capacity
Xinhai improves the traditional specification of crushing chamber by adopting high speed swing jaw and cambered jaw plate.
High-speed hammer impacts materials to crush materials. There are two ways of crushing (Wet and dry)
The cone slide valve is adopted; the failure rate is reduced by 80%; low energy consumption;the separation of different material, improvement of the processing capacity by more than 35%.
Cylindrical energy saving grid ball mill is lined grooved ring plate which increases the contact surface of ball and ore and strengthens the grinding.
20-30%. Rolling bearings replace slipping bearings to reduce friction; easy to start; energy saving 20-30%
Both sides of the impeller with back rake blades ensures double circulating of slurry inside the flotation tank. Forward type tank, small dead end, fast foam movement
Yields from 99.3 up to. 99.5% overall sulfur recovery, without any further tail gas cleanup, are possible. special catalyst which efficiently converts the remaining H2S in the presence of water vapor and 4 barg steam th. –. 2.8. 40 barg
Yields up to 99.2% overall sulfur recovery, without any further tail gas cleanup, are by means of special catalyst which efficiently converts the 4 barg steam.
Jul 31, 2018 Specifications of the feed entered into the first catalytic reactor Comparison of simulation . tration on the reaction furnace temperature and sulfur recovery. First, the simulation of . Pressure bara. 1.38. Temperature °C.
Jun 30, 2004 CrystaSulf is a nonaqueous sulfur recovery process that removes H2S of direct oxidation catalyst in the inlet gas stream to oxidize a portion of the inlet H2S. bar and 250°C 482°F, this corresponds to an actual gas flow
in increasing sulfur recovery and The selective oxidation catalyst in the final reactor oxidizes the H2S to sulfur at an efficiency of more 4 barg steam th. –.
Keywords: sulfur recovery, gas processing, environmental protection , modified Claus process, tailgas cleanup processes. 1. pass through a series of catalytic converters, each of which pressure of 0.05 bar and temperatures below. 370°C
important parameters are presented for a typical sulfur recovery unit. waste heat boiler, and a series of catalytic reactors converters . Pressure bar. 225.
Date AppPub Number Status A sulfur recovery plant is provided comprising a primary Claus reactor and a plurality of downstream reactor Each catalytic reactor that alternates between Claus conditions and CBA conditions is associated
Elmo Nasato Goar, Allison & Associates Tyler, Tex. R. Steve MacDougall Hibernia Management & Development Co. Ltd. St. Johns, Newf. Jan A. Lagas
Sulfur recovery refers to the conversion of hydrogen sulfide H. 2 Each catalytic stage consists of a gas reheater, a catalyst chamber, and a condenser.
Key words: Sulfur recovery, acid gas, Claus process, flameless or colorless combustion catalytic stages is produced and the contaminants such as ammonia
Apr 4, 2015 Sulfur recovery is an important industrial process for fossil fuel clean consumption, sulfur by washing the flue gas and H2S with liquid catalyst
Phoenix Equipment Corporation has this used sulphur recovery unit from a A catalyst is used to facilitate the continued conversion of SO2 to elemental sulfur
Dec 26, 2014 The desorbed H2S is recycled to the Claus unit for sulfur recovery using the According to Bars et al., 10 wt % V loading is the theoretical
Dec 19, 2014 Two catalytic stages will generally give 94-95% sulfur recovery while three . the DP down to < 0.25 bar based upon 3-5 mm catalyst pellets.
Jun 5, 2016 from the integrated Claus sulfur recovery and tail gas treatment units is in the excess of .. In the catalytic reactor, H2S and SO2 will again react and produce gas removal unit at 43 oC and 1.56 bar is sent to the sulfur plant.
Feb 24, 2013 of various acid gas contaminates on the design of a sulfur recovery facility. .. catalyst deactivation and low sulfur recovery as a result of BTEX in the Ambient Conditions: 100ºF 38ºC Maximum, 14.7 PSIA 1.013 bara.
Specific processing requirements such as minimum sulfur recovery and prod- uct quality, . can result in equipment corrosion, catalyst deactivation, and plugging of piping .. line, and overhead access must be provided to rod the seal.
Sulfur Recovery Catalyst provided by the Pingxiang BaiSheng Chemical Packing Bar. Φ4-6. Sphere. Φ3x4-15. Trifolium. Color. White. White. White. Brown.
Nov 11, 2010 PSR Sulfur Recovery Catalyst is used to treat with the acid gases Sphere. Bar. Sphere. Trifolium. Color. White. White. Brown. Blue. Chemical.
Jul 4, 2018 catalysts for sulfur recovery Klaus process; О4-11* catalysts for sulfuric acid production; SELOP technology and Pd-based catalysts for the
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