168results about How to "Reduce gas velocity" patented technology

The present invention concerns a process and an apparatus for thermal conversion of biomass and organic wastes. According to the invention, the feedstock is fed into a fluidized-bed reactor, wherein the feed is converted at an elevated temperature under the influence of particulate matter kept in a fluidized state by a fluidizing gas, the particulate matter is transferred from the reactor to a regenerator for regeneration and then recirculated to the reactor after the regeneration, and the converted hydrocarbon products are recovered from the reactor. Both the reactor and the regenerator comprise risers having an axially annular cross section and being equipped with multi-inlet cyclones for the separation of particulate matter. By means of the invention, it is possible to producer pyrolysis oil, the quality of which is higher than that of oil produced with the processes of the prior art. The incorporation of multi-inlet cyclones into the reactor configuration reduces gas velocities, reduces the physical size of the cyclone and shortens the residence time of gases in the cyclone.

A recoil and muzzle blast dissipator may be attached to the barrel of a gun and may redirect propellant gasses. In one embodiment, a recoil and muzzle blast dissipater may include a body portion having an internal plenum and a plurality of vent slots, each vent slot having an aperture in communication with the internal plenum. Each successive vent slot may include an aperture that is larger in area than the aperture of the previous vent slot. An exterior tube may include a side port and may be arranged to overlay the body portion such that a portion of each vent slot is covered by the exterior tube, and a portion of each vent slot is in communication with the side port.

A method of continuously capturing BioOil and its constituents from a gas stream produced in a fast pyrolysis/thermolysis process, in a usable liquid form so as to produce a non-condensable gas free of fouling contaminates. The method includes separating BioOil and its constituents from a gas stream using hot inertial separation to maintain the temperature of said BioOil and its constituents above a temperature at which the thick and/or sticky constituents cause inefficient operation of the equipment but low enough so that they do not undergo rapid degradation. Next the gas velocity is reduced to a temperature sufficiently low to allow droplets in the gas stream to settle out but high enough so that a viscosity of said droplets remains low enough to avoid inefficient operation of the separation equipment. Finally, liquid is condensed out of the gas stream.

The invention relates to a reactor system and process for the catalytic polymerization of olefin monomer and optionally comonomer(s), having one or more inlets for olefin monomer, catalyst, optionally for comonomer, chain growth controllers or chain transfer agents, and/or inert gas, an outlet for gas and an outlet for polymerized particles. The reactor system has at least one fluidized bed unit and at least one moving bed unit, wherein the fluidized bed unit has means for maintaining a fluidized bed in the fluidized bed unit and wherein the moving bed unit is provided with an inlet and an outlet which are connected to the fluidized bed unit, wherein the outlet of the moving bed unit is provided with means for displacing metered quantities of polymerized particles from the moving bed unit into the fluidized bed unit, and to the use of such reactor system.

A gas cooling type vacuum heat-treating furnace according to the present invention, includes a gas cooling furnace comprising a cooling chamber in which an article to be heat-treated is stationarily set, and defining therein a gas passage in a vertical direction, a gas cooling and circulating device for cooling and circulating gas flowing in the cooling chamber, a gas direction switching device for alternately changing over directions of gas vertically passing through the cooling chamber, and upper and lower straighteners blocking upper and lower ends of the cooling chamber, for causing a velocity distribution of the gas to be uniform.

The invention relates to a waste gas purification tower which comprises a purification tower body; the top of the purification tower body is provided with an exhaust hole; an air inlet hole is formed in one side surface of the bottom of the purification tower body; the purification tower body is internally and sequentially provided with a spray layer, a dehydration layer and an activated carbon layer from bottom to top; a photolysis purifier is arranged above the activated carbon layer; the bottom of the purification tower body is provided with a water storage device; a water outlet hole of the water storage device is connected with a water purification device; a water outlet hole of the water purification device is connected with a spray pipe in the spray layer. Larger particles of dust can be left on a filter screen, the speed of waste gas entering the spray layer is slowed down, small particles of the dust can be reserved by spraying, oil fume in the waste gas can be decomposed by the photolysis purifier, and formed carbon dioxide and water can be directly discharged outside; after the waste gas purification tower is adopted, the odor and bacteria in the waste gas can be removed, the waste gas is not required to be purified for a second time after being purified and can be directly discharged into the air, and the environment is not polluted.

The invention relates to a CO boiler having the dustproof function and the denitration function. The CO boiler having the dustproof function and the denitration function comprises a flue, a combustion chamber, steam drums, an evaporation section and an economizer section. The CO boiler further comprises an ammonia spraying and mixing mechanism and a dustproof denitration reactor. The ammonia spraying and mixing mechanism is arranged above the evaporation section or between the evaporation section and the denitration reactor. The dustproof denitration reactor is arranged between the evaporation section and the economizer section and comprises a mixed-smoke inlet section, a denitration section and a purified-smoke discharging section, wherein an ash removal section is arranged between the mixed-smoke inlet section and the denitration section, ash baffles are arranged in the ash removal section, an ash bin is arranged in the denitration section, the center line of the ash bin and the center line of the reactor coincide, and the lower end of the ash bin is connected with an ash discharging pipeline. According to the CO boiler having the dustproof function and the denitration function, the denitration reactor is arranged in the CO boiler, so that the utilization rate of smoke heat is increased; due to the fact that the ash removal section is arranged in the reactor, smoke dust of mixed smoke can be removed before the mixed smoke enters denitration units, catalyst hole channels are prevented from being blocked, and the denitration efficiency and the denitration effect are improved.

A gas generator for a vehicle passenger protection device. The gas generator includes a combustion chamber in which a gas-generating charge is arranged. A conical deposition chamber is provided that has a first wall, within which a plurality of gas through-holes are formed, and at least one second wall which extends at an angle from the first wall and within which at least one blow-off hole is formed. Gas generated inside the combustion chamber enters the deposition chamber through the gas through-holes and leaves the deposition chamber through the at least one blow-off hole.

A coating device for coating a medical device with a drug-eluting material uses an in-process drying station between coats to improve a drug release profile. The drying station includes a dryer having a telescoping plenum which provides a drying chamber for the stent or scaffold to reside while a heated gas is passed over the stent/scaffold. The drying chamber improves efficiency in drying, predictability or drug release rate, uniformity of coating material properties lengthwise over the stent/scaffold and provides a platform that can effectively support stents that are over 40 mm in length.

The invention discloses a flue gas desulfurization and regeneration integral tower and a flue gas desulfurization method. The flue gas desulfurization and regeneration integral tower comprises a fluegas discharge zone, a demisting zone, a secondary spraying zone, a liquid holding groove zone, a primary spraying zone, a quenching cooling zone and an absorbed liquid regeneration zone, wherein the absorbed liquid regeneration zone is divided into a preheating zone, a steam stripping zone and a liquid collection ozone from left to right in sequence by using a vertical partition plate I, a partition plate II and a partition plate III; the preheating zone communicates with the primary spraying zone; the preheating zone communicates with the steam stripping zone through an opening in the bottomof the partition plate I; the height of the partition plate II is lower than that of the partition plate I; the steam stripping zone communicates with the liquid collection zone through a space at theupper part of the partition plate II; at the tops of the steam stripping zone and the liquid collection zone, the steam stripping zone and the liquid collection zone are completely partitioned from the spraying zone through the partition plate III; a heat exchange tube group is arranged in the preheating zone; a flue gas is fed into a tower through the heat exchange tube pipe; and an outer sleeveis arranged at the top of a chimney arranged in the flue gas discharge zone. The tower is capable of achieving SO2 recycling and deep demisting in the flue gas, is short in process course, simple inequipment and low in operation cost, and has wide application prospects.

The invention discloses a flame holder and a ground gas turbine combustion chamber with the same. The flame holder comprises a central ring and a plurality of radial struts fixed on the outer circular face of the central ring along the radial direction uniformly. A ring body of the central ring and the radial struts are formed by members in groove structures, and groove opening directions of the central ring and the radial struts are identical. Gas flow channels are formed in the members in groove structures and are communicated with the outside through a plurality of gas spray holes in the bottoms of the grooves. The gas flow channel in the central ring and the gas flow channels in the radial struts are communicated to form a gas flow cavity with the shape corresponding to the shape of the flame holder. By means of the flame holder, fuel gas can be burnt stably on the flame holder even under the impact of high-speed gas flows.

The invention relates to a rectification method for propylene and propane separation. The apparatus comprises a multiple heat pump rectification system including a whole tower heat pump distillation system, a rectification system of a rectifying section and a heat pump rectification system of a stripping section, also comprises a tower top stream reflux pump, a stream reflux pump of the rectifying section and a stream reflux pump of the stripping section. Liquefied hydrocarbon enters into a propane and propylene rectification tower from a liquid hydrocarbon concentrate pump through a liquefied hydrocarbon tank; propylene is discharged from the tower top, and propane is discharged from the tower bottom; the propylene concentration at the tower top is 99-99.9%, and the propylene concentration at the bottom of the tower is 1.5-3%; a novel staggered structured packing of window diversion structured packing in highly alternate arranged optimizes radial distribution of the gas and liquid in the rectification tower, buffers the gas phase flow among the filler plates, and plays the role of collecting liquid flow, so as to improve the separation efficiency of propylene and propane. The multiple heat pump rectification system optimizes energy coupling among gas streams in the tower, and reduces energy consumption; and compared with the traditional method, the apparatus reduces the energy consumption by 30% and the total investment for the process.

Disclosed herein is a system for enhancing the recovery of gas in a perforated interval of a gas well. The system features a tubing string having a dead string attached for reducing the flow area of the annulus in the perforated interval, thereby reducing the critical velocity of the gas, i.e., the velocity required to overcome backpressure due to fluids in the well column. The system includes a ported member for receiving gas from the annulus into the tubing string. The ported member and the dead string are isolated from each other by a retrievable plug. The disclosed system provides access from the surface through the dead string for diagnostic or corrective operations. The system also provides delivery of reagents such as foamers to the perforated region to further reduce the critical velocity.

The invention discloses a flue gas dedusting and desulfurizing tower and a flue gas dedusting and desulfurizing method. The flue gas dusting and desulfurizing tower comprises a pretreatment unit, an advanced treatment unit and a tower bottom liquid tank area, and the pretreatment unit is communicated with the advanced treatment unit by a flue gas pipeline. The pretreatment unit sequentially comprises a quenching and spraying area, a first-stage spraying area and a Venturi grating washing area from top to bottom; and the advanced treatment unit sequentially comprises a middle liquid tank area,a second-stage spraying area, an upper liquid tank area, a third-stage spraying area, a demisting area and a flue gas discharging area from bottom to top. The white smoke phenomenon of wet desulfurization is eliminated, so the white smoke phenomenon of a smoke discharging opening is significantly reduced; and the triple functions of flue gas dedusting, desulfurizing and advanced demisting are achieved in the tower, and all functional areas cooperate with each other and promote each other, so the occupied area of the tower is greatly reduced, and the cost for construction and reconstruction ofthe tower is significantly reduced.

Fouling in the scrubber section of a fluid coker unit is reduced by providing baffles to improve the uniformity of the gas flow profile in the scrubber by reducing the gas velocity of the cyclone outlet gases in the scrubber section of the unit. These baffles are located with the objective of reducing the rotational component of the gas flow in the scrubber created by the alignment of the gas outlets of the cyclones. The baffles are preferably located in the shed section of the scrubber and comprise upstanding perforated plates located at the periphery of the scrubber section to disrupt high velocity gas jets in the region of the interior wall of the scrubber.

The present invention discloses a flow baffling type demister, which comprises a plurality of demisting assemblies aligned in parallel, wherein each demisting assembly comprises a gas rising pipe and an outer cylinder, the outer cylinder is arranged on the outer side of the gas rising pipe and is at the same axis line as the gas rising pipe, the gas rising pipe is fixed on a tower disk, the top portion of the gas rising pipe is provided with a sealing cover plate, the circumference of the gas rising pipe is provided with a plurality of seams, the gas rising pipe circumference close to each seam is provided with tangential diversion wings, and the outer cylinder comprises the straight cylinder section on the upper portion and the taper cylinder section on the lower portion. According to the flow baffling type demister, the separation of the liquid droplet and the gas is achieved through the flow baffling during the fluid flowing process; and the flow baffling type demister has characteristics of simple structure, easy installation and effective gas-liquid separation achieving, and is suitable for the gas-liquid separation process in the fields of chemical industry, environmental protection, and the like.

The invention discloses a crude oil distillation method. A primary flash distillation tower is arranged between a normal pressure distillation tower and a pressure reduction furnace, a pressure reduction oil line from an outlet of the pressure reduction furnace to a pressure reduction distillation tower is omitted, a secondary flash distillation tower is arranged between the pressure reduction furnace and the pressure reduction distillation tower, tower bottom heavy oil of the normal pressure distillation tower, i.e. normal bottom oil enters the primary flash distillation tower after being mixed with cyclic pressure reduction slag oil, the tower top gas phase of the primary flash distillation tower is converted into a liquid phase to be used as products through heat exchange and condensing, bottom oil of the primary flash distillation tower enters the secondary flash distillation tower through being heated by the pressure reduction furnace, the tower top gas phase of the secondary flash distillation tower is converted into a liquid phase to be used as products through heat exchange and condensing, and bottom oil of the secondary flash distillation tower is introduced into a flash distillation section of the pressure reduction distillation tower for pressure reduction distillation. Compared with the prior art, the method has the advantages that on one hand, the yield of the pressure reduction slag oil is reduced, and the economic benefits of devices are improved; and on the other hand, the load of the pressure reduction furnace and the pressure reduction distillation tower is reduced, the device investment is saved, and the energy consumption of the devices is reduced.

The invention relates to a vertical mill for grinding a product to be milled and a method therefor, wherein the vertical mill has a grinding plate and one or more grinding rolls. A blade ring annular channel is provided for a transport gas flow rising around the grinding plate. An annular gap is provided between a downwards projecting middlings cone and the upper range of the grinding rollers through which gap even a fines content is recirculated back to the grinding plate. To overcome this disadvantage, a barrier gas flow is provided flowing from the inside towards the outside, by means of which the recirculation of ground particles of a defined size can be prevented.

The invention discloses a flue gas desulfurizing tower and a flue gas desulfurization and wastewater treatment method. The flue gas desulfurizing tower sequentially comprises a flue gas exhaust area,a demist area, a tower tray area, a spraying area and a wastewater treatment area from top to bottom; the flue gas exhaust area and the demist area are connected through a cone deformation diameter, the tower tray area and the spraying area are connected through an inverted cone deformation diameter; the wastewater treatment area is divided by a vertical partition plat I from the center into an oxidation flocculation area and a circulation clear liquid area, the circulation clear liquid area is completely separated from the oxidation flocculation area and the spraying area through a partitionplate II from the top part of the circulation clear liquid area; the oxidation flocculation area is provided with a stirring device; and the vertical partition plate I is provided with a filter medium. The flue gas is subjected to dust removal, desulfurization and wastewater treatment in one tower, the flue gas is used to stir the wastewater to implement the operations of oxidation flocculation and concentration, the difference of the liquid levels of the two sides of the vertical partition plate is used as a driving force to filter the desulfurization wastewater, the occupied area is greatlyreduced, and the costs for the construction and transformation of the device and the operation cost of the device are obviously lowered.

In some embodiments, a gas diffuser for use in a mass spectrometer is disclosed that can provide a controlled expansion of an ion-containing gas so as to reduce gas velocity for entry into subsequent stages of the mass spectrometer, e.g., a mass analyzer. In some embodiments, the controlled expansion of the gas is provided by flowing the gas through a channel whose cross-sectional area change, e.g. progressively increases, in the direction of the gas flow so as to provide controlled expansion of the gas.

The invention discloses a gas-liquid distributor with support and mass transfer function, which consists of multiple liquid phase distributing grooves to arrange parallelly along radial direction and multiple liquid phase distributing semi-grooves on two sides of liquid phase distributing groove, wherein each gap of liquid phase distributing groove and semi-groove is gas phase distributing channel, which interconnects each liquid phase distributing groove and semi-groove, the mass transfer hole is opened on the liquid phase distributing groove and semi-groove, which is compatible with mass transfer function for distributor.