Abstract: An apparatus and method are provided in which a vaporizer vaporizes a liquid feed for introduction to a feed conversion unit such as a steam active reformer. A condenser condenses vaporized feed from the vaporizer when introduction of feed to the feed conversion unit is stopped. Condensed, liquid feed is passed back into the vaporizer and is conserved rather than going to flare.

Abstract: A process for the removal of CO.sub.2 and sulfur compounds from natural gas and raw synthesis gas wherein N-formylmorpholine and N-acetylmorpholine mixtures are used as the desorbent at temperatures between -20.degree. C. and +40.degree. C. at pressures of 10 to 150 bar in a scrubbing operation. The acid gases are removed from the absorbent by flashing and the regenerated absorbent is recycled to the absorbent.

Abstract: Process for the recovery of pure hydrocarbons from a hydrocarbon mixture, more particularly, a high aromatics content hydrocarbon mixture, by extractive distillation in an extractive distillation column. A first solvent feed for a first sub-flow of a selective solvent is provided between the top part of the column and the bottom part thereof. The selective solvent used is an N-substituted morpholine. Substantially non-aromatics are withdrawn as the raffinate from the head of the extractive distillation column and substantially aromatics and selective solvent are withdrawn as the extract from the sump of the extractive distillation column. A second sub-flow of the selective solvent is introduced via a second solvent feed in the top part of the column above the first solvent feed. The quantity of solvent supplied with the second sub-flow constitutes less than 50% of the total quantity of solvent.

Abstract: The present invention relates to a method of and an apparatus for treating of textile substrates with a supercritical fluid. The textile substrates are formed as spools of yarn or rolled webs, and the supercritical fluid flows over and/or through them substantially perpendicular to their spool or winding axis. At that, the treatment temperature assumes different values during the treatment period. It is provided that during the treatment period, the treatment temperature values are set by at least two functions of the treatment time, and that the supercritical fluid is conditioned differently at the time the following function takes effect.

Abstract: A device for feeding a gaseous fluid radially from a center of a vessel outwards, including a central vertical gas feed tube having at least one vertical row of discharge openings, a catalyst bed of bulk material accommodated in a perforated basket, which includes a perforated cylindrical surface surrounding the central vertical gas feed tube in a spaced relationship thereto and defines with the guide feed tube a hollow cylindrical space, the perforated cylindrical surface defining an impingement surface of the catalyst bed, and deflector elements provided at the at least one row of the discharge openings to insure a substantially tangential flow of gas into the hollow cylindrical space.

Abstract: A high-pressure generating apparatus including a high-pressure chamber, a low-pressure chamber located beneath the high-pressure chamber and having a diameter substantially larger than the diameter of the high-pressure chamber, a tandem piston having first and second portions displaceable in the high-pressure and low-pressure chambers, respectively, for building-up pressure therein, and a yoke embracing the high-pressure and low-pressure chambers for applying a pressure force to the high-pressure chamber cover and the low-pressure chamber bottom upon built-up of pressure in the high pressure and low-pressure chambers.

Abstract: A process for the partial oxidation of bituminous oil emulsions to produce a raw gas containing CO and H.sub.2, the process including heating the bituminous oil emulsion to destabilize the emulsion and separating the bituminous oil from the emulsion water, concentrating the emulsion water by evaporation, and reacting in a gasification unit the bituminous oil, the concentrated emulsion water and oxygen or air to produce the raw gas containing mainly CO and H.sub.2.

Abstract: A resonant vibrating conveyer is disclosed which has a vibratory drive and spring supports connecting the trough with an intermediate frame which is, in turn, attached to a foundation via springs. The forces transmitted to the foundation are reduced to a minimum while permitting a relatively light-weight construction of the conveyer. This is achieved by arranging first pre-loaded springs with countervibrating masses acting at the point of attachment of second pre-loaded springs between the conveyer trough and the intermediate frame.

Abstract: A device for the generation of synthesis gas with a plurality of catalyst-filled reformer tubes suspended in a pressure vessel, the reformer tubes being at least partially enveloped by jacket tubes intended to conduct product gas in an upward direction from a lower mixing chamber into the head space of the pressure vessel, the intended purpose of said device being to provide a solution, in particular for improving the mixing of the ensuing streams while simultaneously equalizing the heat transfer by mechanically simple and economical means.This is achieved by making the jacket tubes protrude beyond the ends of the reformer tubes thus forming an individual mixing chamber for each reformer tube.

Abstract: The formation of dust or fines may be suppressed, during the granulation of ammonium nitrate having a nitrogen content of 28% to 34.5%, by a process in which ammonium nitrate is initially granulated to form a raw granulate containing fines, and thereafter heated and contacted by a hydrated sulfate during a second granulation step wherein the fines are affixed to the raw granulate.

Abstract: A process and apparatus for extracting ingredient substances from natural products by means of a pressurized fluid, particularly for decaffeinating tea leaves by means of carbon dioxide, wherein the ingredient substances are bound by an adsorbent, preferably activated carbon. The fluid is conducted through a product layer, the thickness of which in flow direction is small in comparision with that transversely of the flow direction and the fluid is passed through the product layer with changing, especially increasing, velocity. The apparatus includes a cylindrical high-pressure vessel with annular cylindrical baskets for accommodating the natural product and/or the adsorbent, and the gas flows from a cylindrical outer range to a cylindrical inner range. The time required for the treatment of leafy natural product is reduced, the flow paths of the fluid are shortened, thus diminishing the risk of clogging, and the fluid flow velocity is reduced.

Abstract: A device for accommodating catalyst in particular a primary and a secondary catalyst in the production of synthesis gas in an auto-thermal reformer has the primary catalyst being accommodated in a plurality of catalyst tubes, providing an optimal, and above all, compact design, guaranteeing sustained optimum gas flow and expansion properties in the context of an overall exothermic reaction. This is achieved in that each individual primary catalyst tube (11) correlates with an individual secondary catalyst and that the primary catalyst tube (11) continues in the form of a narrow feed tube (11a) that extends through the respective secondary catalyst (13).

Abstract: A process and an apparatus for the purification of gases, particularly for the desulphurization of and NO.sub.x -elimination from flue gas by multistage adsorption and catalytic reaction in gravity-flow moving beds of granular, carbon-bearing materials contacted by a transverse steam of the gas, in which a minimum of two moving beds are arranged in series with reference to the gas route so that NO.sub.x -elimination takes place in the second or any downstream moving bed. Where large volumes of flue gas from industrial furnaces must be purified, purification is adversely affected by the formation of gas streaks with widely varying sulphur dioxide concentrations. This disadvantage is eliminated in that the prepurified flue gas leaving the first moving bed and having a locally variable sulphur dioxide concentration gradient is subjected to repeated mixing before ammonia is added as reactant for NO.sub.x -elimination.

Abstract: A process is disclosed whereby the recovery of process heat contained in NOx gases which have been generated by the combustion of ammonia in the ammonia oxidation step of a nitric acid production process is improved and whereby the recovery of the process heat takes place at a low temperature range. The process involves using process heat contained in NOx gases to evaporate and superheat liquid ammonia which is circulated in a separate loop, then expanding the superheated ammonia in a turbine to generate mechanical energy and subsequently pressurizing, reevaporating and resuperheating the ammonia.

Abstract: A device for separating coarse and/or fine particles from raw gas, including a filter shell with an inlet and an outlet for bulk material, granular bed filters reaching into the raw gas inlet duct, and purified gas outlets communicating with a common outlet duct.

Abstract: Bulk material containing vaporizable ingredients, such as lignite, hard coal, peat, waste wood, clarifier sludge, waste sludge, contaminated earth, catalysts, zeolites and filter cake, is conditioned by means of a vibrating plate conveyor divided into a heating section and a drying section, using an indirect heat exchange method. The bulk material is heated in an enclosed heating section while withdrawing the vapor from this section. In the downstream enclosed drying section, the vaporizable fractions contained in the bulk material are further reduced with the aid of heat supplied indirectly, the vapor being withdrawn. The bulk material is separated several times into coarse and fine fractions utilizing at least one slotted grid, the fines being immediately recycled and remixed with the coarse fractions which have a higher water content. The bulk material is mixed several times while being heated in the drying section before discharge.

Abstract: A process for the generation of mechanical energy in the ammonia oxidation step of process for the production of nitric acid is disclosed, whereby the utilization of process heat is improved, particularly the exploitation of heat contained in NO.sub.x gases and including process heat recovered at low temperature. The process involves evaporating and superheating liquid ammonia upstream of the oxidation step, at a pressure which is a multiple of the pressure required for the combustion, using the process heat of the NO.sub.x gases formed during the the combustion and then expanding the superheated ammonia in a turbine, thus generating mechanical energy.

Abstract: The invention relates to a reactor for industrial plants, e.g. for an ammonia synthesis plant, comprising several catalyst beds in series charged by a radial gas flow. The object is to provide for a uniform gas flow through the catalyst bed along its entire height, otherwise different space velocities are experienced within the catalyst bed involving irregularities in the reaction. The problem is solved when the cross-section of the annular space for the effluent reaction gas flowing in axial direction is equal to or larger than the cross-section of the annular space for the influent fresh gas flowing in axial direction.

Abstract: The invention relates to a device for clamping and unclamping of components with the aid of a clamping flange, at least one of said components being clamped by the hook of said device, the clamping force being transferred via a bolt linked with the hook and a nut that can be operated from the external side. The invention provides for a device clamped and unclamped by means of a tool such as an impact wrench, the head of which need not be tilted, lifted or lowered.The aim of the invention is achieved by means of nut (5) that is arranged in a fixture and that can be turned but yet remains in a defined position, and by means of hook (10) that is linked with bolt (6) and guided with the aid of element (12) in groove (11) of fixture (5), the hook thus performing upward and downward motions and being swivelled by at least 45.degree. around its longitudinal axis for unclamping the flange.

Abstract: Bulk material containing vaporizable ingredients, such as lignite, hard coal, peat, waste wood, clarifier sludge, waste sludge, contaminated earth, catalysts, zeolites and filter cake, is conditioned by means of a vibrating plate conveyor divided into a heating section and a drying section, using an indirect heat exchange method. The bulk material is heated in an enclosed heating section while withdrawing the vapor from this section. In the downstream enclosed drying section, the vaporizable fractions contained in the bulk material are further reduced with the aid of heat supplied indirectly, the vapor being withdrawn. The bulk material is separated several times into coarse and fine fractions utilizing at least one slotted grid, the fines being immediately recycled and remixed with the coarse fractions which have a higher water content. The bulk material is mixed several times while being heated in the drying section before discharge.