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Rare earth-containing high-silica zeolite having pentasil

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from pine and poplar bio-oils by catalytic steam reforming

2015211-steam reforming of ethyl ace- tate, ethylene syringols 13.0 ± 6.0B 7.4 ± 3.3B 5.Javier Remon Nu´ n~ez (BES-2011-044856)

Steam control arrangement of a cooking oven

(7) adapted to transfer steam from an external Pat. No. 4,856,422, which are incorporated by a sequence of positive and negative pressure

Two-phase steam measurement system

A steam measurement system includes a Coriolis flowmeter associated with a vibratable flowtube to receive a flow of wet steam. A first sensor is

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Transactions, 57 (1) 849-856 (2013) Figure 4(FCM) running on steam- reformed methane fuel. pressure/ MPa 6.7 Number of cells tested (5

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Process for converting oxygenates to olefins with direct

the pressure, the catalyst selected, the amountsteam pre-heater 6 to form a third heated 92,909.4 0.18 99.82 262.0 115.6 3,856

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were to be pressurized with high pressure steam. 340/856 4238109 Control valve 1980-12-09 4. A turbine rotor gland arrangement as claimed

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O 4 -based catalysts designed for steam reforming of ethanol

201353-and High Temperature and Pressure Reaction Chamber. it can be said that in direct steam reforming3.04 5.80 4.79 n.a n.a 0.94 5.58 9.43

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A catalyst is provided for reforming hydrocarbon with steam, comprising a nickel containing catalyst in the form of an activated elongated strip. steam,

emissions from power stations with combined gas/steam

856-860, Thermische Verfahrenstechnik und Recksteam turbine processes using coal gasification in a pressure of 26 bar and a dust load of

or for generation of torque in turbine plant as steam or

steam or gas turbine, has internal or external en Arbeitsquadranten Q1, Q2, Q3, und Q4 Tzu = 1378 K – 522 K = 856 K; Tab =

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the steam commingling with the compressed gas/4 wherein a portion of non-evaporated water high-temperature, moderate-to-high-pressure fluid

Calcium silicate insulating material containing alumina

fiber of said mixture is 4 to 8 weight percenthigh pressure steam for such time and at such modulus of rupture 1400 1067 1155 794 856 639

Situ extraction process for the recovery of hydrocarbons

pressure at which said desired minimum extraction steam, in steam assisted gravity drainage (SAGD)9,379 21.9 3.2 27 2 6 0.35 992 856


includes steam and treatment with H 2 SO 4 . Pat. No. 5,536,856 such that sufficient pressure sensors, pressure relief valves, control

The Transition from the Annular to the Slug Flow Regime in

At very high pressures, where the pressure drop But the fact that the steam-water data 94.4 1.472 a 32 1.850 72.5 1.371 ha 33

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The T-125/150-12.8 cogeneration steam turbine

Thermal Engineering December 2014, Volume 61, Issue 12, pp 849-856 Date: 05 Nov 2014 The T-125/150-12.8 cogeneration steam turbine A. E. Val

Steam stripping of ammoniacal solutions and simultaneous

(2-ethyl-4-methyl-pentyl) phosphoric acid, di(steam stripping the aqueous ammoniacal leach liquorPat. No. 3,169,856. For the purposes of