Products

B3steam dryer y hose supply

Plate type steam reformer

Disclosed is a plate type steam reformer comprising a plate type burner capable of heating a broad area of a reactor as a heat source, positioned on

Steam reforming catalyst and a method of preparing the same

2001419-A catalyst for the steam reforming of hydrocarbons into gases such as methane, hydrogen and carbon monoxide and a method of preparing the sa

HYDROGEN GENERATION APPARATUS

International Classes: C01B3/38; B01J7/00 View steam; a combustor configured to combust a supplied with heat from the reformer, and cause

ZEOLITE MEMBRANES FOR SELECTIVE OXIDATION ON CARBON MONOXIDE

B01J37/02; C01B3/50; C01B3/56; C01B3/58Y-type zeolites may preferably utilized as the the presence of steam and other relevant

Process for reducing concentration of carbon monoxide in

B01J23/656; B01J23/89; C01B3/58; (IPC1-7(a) subjecting hydrocarbons or methanol to steamAfter drying, the obtained Mn/Pt-supporting

Small cylindrical reformer

steam to produce hydrogen, said catalyst consistingto extraction thimble (68) via hose clamp (69) C01B3/10, C01B3/063, Y02E60/36,

apparatus and method operable without supply of steam and

A hydrogen production apparatus is disclosed which operates based on a steam reforming method and operates without supply of steam from outside. The

the flow rate of fuel vapor and oxygen to be supplied into

2002131-supplied into said fuel reformer and of second the flow rate of steam in relation to the Y02E60/50, C01B2203/1276, C01B2203/044,

Flash dryer for drying a fibrous tobacco product

A24B3/18 A24B3/12 F26B17/103 F26B2200/22 drying a fibrous tobacco product (16), having asteam jets 20, 17 so that a rotating beam

angled downwards in a rotating drying tube with hot steam

Evapn. dryer for fibrous pressed material, esp. sugar beet scraps, has a rotating contact drying tube (10) with a number of parallel tubes (11)

MEETING OF THE SUBCOMMITEE ON POWER UPRATES ROOM T-2B3,

2B3, 11555 ROCKVILLE PIKE, ROCKVILLE, MD October 9-10, 2007 Susquehanna Steam Dryer and Vessel Internals ***** BREAK **** ******* CLOSED

#x03B3;-Al2O3 catalyst on the steam reforming of acetic acid

Effect of calcination temperature of Ni/amp;#x03B3;-Al2O3 catalyst on the steam reforming of acetic aciddoi:10.1109/SUPERGEN.2009.5348046

PROCESS FOR PRODUCING A FOAM MOLDING

2006715-pAfter heating the expandable resin beads to sealing temperature of expandable resin beads in the presence of heated steam, foam cells are

REVERBERATORY FURNACE USING WASTE GAS FOR COMBUSTION

20061119-This disclosure involves a reverberatory furnace installation including a steam generating system in which auxiliary steam for the process i

COAL DRYING APPARATUS USING LOW-PRESSURE SUPERHEATED STEAM

dryer formed by including a first dryer to whichsteam is supplied from the superheater in order F26B21/02; C10B57/10; F26B3/084; F26B15/

Process for recovering olefins

steam, carbon dioxide, carbon monoxide, methane,a dryer 119 to remove residual water therefrom. C01B3/501, F25J2270/90, F25J2205/80, F25

Plant for the production of hydrogen and of energy

B01D71/56; B01D53/04; C01B3/36; C01B3/48; C01B3/50; C01B3/56;(or another incoming hydrocarbon gas supply), or else to a steam

INSTANTANEOUSLY COMPLETELY COMBUSTIBLE CARTRIDGE CASE MEMBER

F42B3/28; F42B5/18; F42B5/188; F42B5/drying the cylinder before removing it from the thereafter stopping the supply of the steam,

Steam generator

A steam generator includes a tank having an inlet in a lower part for feeding a fluid, and an outlet in an upper part for discharging a vapor-

Device for replacing air within a container headspace

B65B3/18; B65B31/04; B67C3/22; (IPC1-7): B65B31/02 a steam supply and at least two inert gas supplies; at least one

Steam cocker

When water supply based on the temperature detected by the water temperatureWO2006013771A1 Jul 28, 2005 Feb 9, 2006 Ando Yuji Steam cocker

Flash dryer for particulate materials

2009320- A24B5/00; F26B1/00; A24B3/04; F26B3/10;steam and has a drying temperature in the rangethe guide wall 56 as shown by arrows Y in

Catalyst performance recovery method for reforming catalyst

C01B3/32; C01B3/40; H01M8/04; B01J35/04; and a control device for controlling supply (steam/carbon: molar ratio), methanol LHSV=15,

Aseptic filling valve

B65B3/00; B65B39/00; B67C3/26; F16K31steam sterilization or by the action of the valuably used as a fluid control valve to be

Method for thermochemical production of hydrogen from water

2007419- C01B3/02; C01B3/06; C01B13/02; C01B3/00 water is supplied to the second reaction vessel and steam was fed to the reaction vessel at

METHOD OF DISPOSING OF ORGANIC WASTE OF HIGH WATER CONTENT

2011620-(22) a heat exchange of the superheated steam after the drying to thereby C02F11/06; C02F11/12; C04B7/38; C04B7/44; F26B3/06 View Patent