103results about "Liquid degasification arrangements" patented technology

The invention discloses an ultra-aeration air flotation system and an implementation method thereof, and belongs to the technical field of wet-process phosphoric acid production, and the ultra-aeration air flotation system comprises a reaction tank, an inclined guide plate arranged on the inner wall of the reaction tank, a dish-shaped tank which is arranged at the bottom of the reaction tank and is annularly arranged around the center of the reaction tank, and a central island which is formed by protruding the inner ring part of the dish-shaped tank at the bottom of the reaction tank, the aeration mechanism is arranged on the central island and is communicated with the outside through a pipeline; the transmission mechanism is arranged above the reaction tank; the central transmission rod is connected with the output end of the transmission mechanism and is arranged along the axis of the reaction tank; the dynamic settler is arranged at the upper part in the reaction tank and is connected with the central transmission rod; and the overflow port is matched with the dynamic settler. The inclined guide plate, the dish-shaped aeration structure and the dynamic settler are integrally arranged in the reaction tank, so that the super-aeration uniformity, the foam separation capacity, the phosphoric acid purification and the liquid vortex intensity in the wet-process phosphoric acid production process are remarkably enhanced, and the reaction efficiency and the product quality are improved.

The present invention discloses a super-aeration flotation system and its implementation method, belonging to the technical field of wet-process phosphoric acid production. The system comprises a reaction tank, an inclined guide plate arranged on the inner wall of the reaction tank, a dished trough arranged at the bottom of the reaction tank and arranged in a ring shape around its center, a central island formed by a protrusion of the inner ring portion of the dished trough at the bottom of the reaction tank, an aeration mechanism arranged on the central island and connected to the outside through a pipeline, a transmission mechanism installed above the reaction tank, a central transmission rod arranged along the axis of the reaction tank and connected to the output end of the transmission mechanism, a dynamic settler arranged at an upper position in the reaction tank and connected to the central transmission rod, and an overflow port matched with the dynamic settler. By integrating the inclined guide plate, the dished aeration structure and the dynamic settler in the reaction tank, the present invention significantly enhances the super-aeration uniformity, foam separation ability, phosphoric acid purification and liquid vortex intensity in the wet-process phosphoric acid production process, thereby improving reaction efficiency and product quality.

The present invention relates to a heatable partition for a defoliation apparatus for defoliating a composition containing volatile components, such as for defoliating a solid or liquid polymer composition containing unreacted monomers, solvents, and / or by-products, wherein the heatable partition comprises at least one vessel having an upstream portion and an adjacent downstream portion, the upstream portion of the vessel having a first side end having an inlet and a second side end on the opposite side connected to the downstream portion, the downstream portion of the vessel having a first side end connected to the second side end of the upstream portion and a second side end on the opposite side, the downstream portion of the vessel comprising a hollow double plate assembly, the hollow double plate assembly comprising an upper plate and a lower plate arranged in staggered order but separated such that a void chamber is defined between the upper plate and the lower plate, each of both plates having a plurality of openings, each opening in the upper plate being surrounded by a wall extending through the void chamber and surrounding the opening in the lower plate so as to form a plurality of passages that are fluid-sealed and separated from a hollow space defined in the void chamber between the passages, the hollow space being connected to an inlet for a heating medium and an outlet for a heating medium.

A lamp-housing assembly includes a lamp seat with a first contact member, a lamp with axially opposite first and second electric terminals, and a lamp cap with a second contact member. The lamp is insertable into the lamp seat. The lamp cap is mountable on the lamp seat and the inserted lamp. Inserting the lamp into the lamp seat establishes an electric coupling of the first electric terminal with the first contact member. Mounting the lamp cap on the lamp seat and inserted lamp establishes an electric coupling of the second electric terminal with the second contact member. The lamp seat, lamp and lamp cap are matched such that, after insertion and mounting, the lamp is axially and radially aligned and electrically and thermally coupled with the lamp seat and the lamp cap. The assembly may be utilized for a detector of a fluidic sample separation apparatus.

The invention provides a defoaming and sub-packaging method of heat-conducting silica gel. The defoaming and sub-packaging method comprises the following steps: stirring and mixing all materials for forming the heat-conducting silica gel in vacuum according to a set proportion; the stirred mixed material is vacuumized, and then the mixed material is subpackaged into a tank body; carrying out gradient centrifugal defoaming treatment on the mixed material in the tank body; and pressing the centrifuged material into a needle cylinder tube from the bottom of the centrifugal tank to obtain a subpackaged heat-conducting silica gel finished product. According to the invention, the good defoaming effect of the heat-conducting silica gel can be realized, the comprehensive performance such as the heat conductivity of the heat-conducting silica gel is improved, the quality stability of the product is greatly improved, and the production efficiency of the heat-conducting silica gel defoaming process is improved.

This invention provides a gas-liquid separator for separating diazonium methane from a diazonium methane mixture. The separator comprises an upper cylinder, a middle cylinder, and a lower cylinder connected sequentially from top to bottom. The upper cylinder has a gas outlet at its top center, surrounded by gas moisture detection ports, diazonium methane content detection ports, gas temperature detection ports, and an explosion vent. A pressure detection port is located on the side. The middle cylinder has a refrigerant inlet and a refrigerant outlet at its upper part, and a refrigerant coil is installed inside the middle cylinder. The refrigerant coil inlet is connected to the refrigerant outlet, and the refrigerant coil outlet is connected to the refrigerant outlet. The lower cylinder has a liquid level-above gas inlet and a liquid level-below gas inlet at its upper part. The liquid level-above gas inlet is connected to a gas distributor above the liquid level via a pipe, and the liquid level-below gas inlet is connected to a gas distributor below the liquid level via a pipe. A feed inlet is located on the middle side wall of the lower cylinder. This gas-liquid separator offers high gas-liquid separation efficiency, is explosion-proof, and can be used for continuous automated production.

The invention concerns a water sealed tank, comprising : a tank body and a heat conducting pipe. The tank body comprises a gas-liquid inlet, a water outlet and a gas outlet, wherein the gas outlet is close to or located on a top portion of the tank body and communicates with the tank body, the water outlet is close to or located on a bottom portion of the tank body, the gas-liquid inlet communicates with the tank body and is used for feeding a gas-water mixture into the tank body, and a gas separated from the gas-water mixture inside the tank body is discharged from the gas outlet. At least a part of the heat conducting pipe is located inside the tank body, and used for a liquid to flow through, so as to allow the heat conducting pipe to exchange heat with water inside the tank body and heat the water inside the tank body. A water electrolysis process for preparing hydrogen generates a lot of additional heat. By using the heat generated by electrolysis to heat the water inside the water sealed tank, the heat is effectively utilized without adding additional heating facilities in the water sealed tank to increase the water temperature, thereby reducing the waste of energy.

A degassing system for use in dialysis, comprising: a degassing vessel having a fluid inlet, and a fluid outlet; a degas flow restrictor fluidly connected to the inlet of the degassing vessel; a fluid pump fluidly connected to the degassing vessel and located downstream of the degassing vessel, for pulling fluid into the degassing vessel through the fluid inlet and out of the degassing vessel through the fluid outlet; a vacuum pump attached to the degassing vessel for removing gas from the degassing vessel; and. a degas sprayer located inside the degassing vessel at the fluid inlet of the degassing vessel such that fluid entering the degassing vessel through the fluid inlet passes through the degas sprayer.

The invention provides a gas separation device, a gas collection system and a gas collection method. The gas separation device comprises a heating device, the heating device comprises a fixing plate and a heating ring, the fixing plate is an annular plate, the separation container is fixed in the separation cylinder through the fixing plate, and the heating ring sleeves the outer side of the separation container, so that a stable and uniform heating environment can be provided for an oil sample in the separation container; uniform heat conduction in the heating process can be ensured, and the gas release efficiency is improved. The stirring mechanism comprises a driving motor, a stirring shaft, an inclined blade assembly and a spiral blade assembly, and the oil sample can be fully stirred while being heated. The combined design of the inclined blade assembly and the spiral blade assembly can generate strong axial and radial flow, ensures that an oil sample is uniformly heated, accelerates the release and separation of gas, ensures the stability and high efficiency of the separation process, can improve the adaptability of the gas separation device, and improves the use experience.

The present invention relates to a devolatilization apparatus for devolatilizing compositions containing volatile components, such as for devolatilizing solid or liquid polymer compositions containing unreacted monomers, solvents, and / or by-products, the devolatilization apparatus comprising a vessel having at least one inlet for the composition to be devolatilized, at least one outlet for the devolatilized composition, at least one outlet for gas, at least one heatable tray, and optionally at least one heatable distributor, the vessel comprising a hollow vessel having upper and lower plates, at least a section of the at least one heatable tray and / or the at least one heatable distributor arranged one on top of the other but spaced apart such that a void chamber is defined between the upper and lower plates. The vessel comprises a double-plate assembly, each plate having a plurality of openings, each opening of the upper plate being surrounded by a wall that extends through the void chamber to form a plurality of passages that are fluid-tightly separated from hollow spaces defined in the void chambers between the passages and that surround the openings of the lower plate, the hollow spaces being connected to an inlet and an outlet for the heating medium, the upper and lower plates of the hollow double-plate assembly being connected to each other at their sides via side walls that define the void chambers therebetween, and at least one heatable tray and / or at least one heatable distributor extending over 10 to 99% of the cross-sectional area of ​​the vessel and surrounded by a non-perforated weir.

The present invention relates to a devolatilization apparatus for devolatilizing a composition comprising a volatile component, such as for devolatilizing a solid or liquid polymer composition comprising non-reacted monomer, solvent and / or by-product, wherein the devolatilization apparatus comprises a vessel comprising at least one inlet for the composition to be devolatilized, at least one outlet for devo-latilized composition, at least one outlet for gas, at least one heatable tray and op-tionally at least one heatable distributor, wherein at least a section of at least one heatable tray and / or of at least one heatable distributor comprises a hollow dou-ble-plate assembly comprising an upper plate and a lower plate being arranged on top of each other, but spaced apart so that a void chamber is defined there-between, wherein each of both plates comprises a plurality of openings, wherein each opening of the upper plate is surrounded by a wall extending through the void chamber and surrounding an opening of the lower plate so as to form a plural-ity of channels being fluid-tightly separated from the hollow space being defined in the void chamber between the channels, wherein the hollow space is connected with an inlet for heat medium and with an outlet for heat medium, wherein the up-per plate and the lower plate of the hollow double-plate assembly are connected with each other at their sides through sidewalls, between which the void chamber is defined, wherein the at least one heatable tray and / or at least one heatable dis-tributor extends over 10 to 99% of the cross-sectional area of the vessel and is surrounded by a non-perforated weir.

A method for continuously removing a particular type of gas molecules (“gas molecules”) from a gas stream includes selecting a liquid having an affinity for the gas molecules to be removed, and providing the selected liquid to each of a first and second mat, each mat formed from a plurality of fibers having the ability to retain the selected liquid within longitudinally extending channels having longitudinally extending openings against moving into the space between the individual fibers, the mats in fluid communication therebetween with the selected liquid. The method includes directing the gas stream through a portion of the first mat into contact with the selected liquid along the longitudinally extending openings whereby the selected liquid absorbs the gas molecules, and directing a second gas through a portion of the second mat so that the gas molecules, absorbed by and disbursed throughout the selected liquid, are stripped and carried away.

A redox flow acid-gas capture system includes an electrochemical cell including a cathode configured to contact a stream including an electroactive species in an inactive state and provide a reduced stream including the electroactive species in an active state, and an anode configured to contact an adduct stream including an adduct of an electroactive species and an acid-gas and provide an oxidized stream including the electroactive species in the inactive state and the acid-gas; an absorber configured to contact the reduced stream and the acid-gas and form the adduct stream including the adduct of the electroactive species and the acid-gas; and at least one of an oxygen stripper unit, or a degasser unit configured to provide a degassed stream including the electroactive species in an inactive state, and an acid-gas stream.

The present invention relates to the technical field of electrolysis and very particularly to a degassing device for an electrolysis plant for the production of dihydrogen (H2) and dioxygen (O2) by electrolysis of water. According to the present invention, the plant comprises a degassing device (1, 101) which comprises a degassing chamber (14, 114) provided with an opening for a gas-liquid mixture supply pipe (11, 111), with an opening for a a liquid discharge pipe (12, 112) arranged below the level of the gas-liquid interface (15, 115) of the degassing chamber (14, 114), and with an opening for a gas discharge pipe (13, 113) arranged above the level of the gas-liquid interface (15, 115) of the degassing chamber (14, 114). Furthermore, a static mixer (21, 121) is inserted into the gas-liquid mixture supply pipe (11, 111).

One or two continuous recirculation loops are utilized for the well-site equipment that separates produced fluids into sand, liquid, and gas during drill out and flow back that occurs after fracturing a subterranean formation. When one recirculation loop is utilized, the recirculation loop continuously recirculates fluid between the recirculation chamber of the disclosed sand removal apparatus and a shaker device. When two recirculation loops are utilized, the first recirculation loop continuously recirculates fluid between a recirculation chamber of the disclosed sand removal apparatus and a shaker device, and the second recirculation loop continuously recirculates fluid between the recirculation chamber and a gas separator.

The application relates to a vacuum infinite-gas-volume insulating oil gas separation device and method, and relates to the field of power system automation. The device comprises a gas-liquid separation unit and a gas analysis module. The gas inlet end and the gas outlet end of a vacuum degassing chamber in the gas analysis module are connected with the gas-liquid separation unit; the first connecting end of the vacuum degassing chamber is connected with the inlet of a gas collection chamber through a sixth electromagnetic valve and a first gas equalization pump in sequence; the second connecting end of the vacuum degassing chamber is connected with the outlet of the gas collection chamber through a seventh electromagnetic valve; and a pressure sensor is arranged in the gas collection chamber. The oil degassing state in the application is a vacuum state, the vacuum degree is adjustable, and the adjustable range is 10KPa-101KPa. For the concentration of some micro-content gases (such as acetylene, ethane and ethylene) in transformer oil, only in the vacuum state can sufficient amount of the gases be degassed to meet the detection sensitivity of a rear-end detection system.

The present invention relates to a cartridge comprising at least one heatable tray and / or at least one heatable distributor, wherein at least a section of at least one heatable tray and / or of at least one heatable distributor being arranged within the cartridge, at least one support element, on which at least one heatable tray and / or at least one heatable distributor is arranged, one central inlet line for heating me-dium and one central outlet line for heating medium, wherein at least a section of the at least one heatable tray and / or of the at least one heatable distributor com-prises a hollow double-plate assembly comprising an upper plate and a lower plate being arranged on top of each other, but spaced apart so that a void chamber is defined therebetween, wherein each of both plates comprises a plurality of open-ings, wherein each opening of the upper plate is surrounded by a wall extending through the void chamber and surrounding an opening of the lower plate so as to form a plurality of channels being fluid-tightly separated from the hollow space be-ing defined in the void chamber between the channels, wherein the hollow space is connected with an inlet for heat medium and with an outlet for heat medium, and wherein the central inlet line for heating medium of the cartridge is connected with the inlet (s) of the at least one heatable tray and / or at least one heatable distributor, and wherein the central outlet line for heating medium is connected with the out-let(s) of the at least one heatable tray and / or at least one heatable distributor.

The present invention relates to a heatable distributor, in particular for a devolati-lization apparatus for devolatilizing a composition comprising a volatile component, such as for devolatilizing a solid or liquid polymer composition comprising non-reacted monomer, solvent and / or by-product, wherein the heatable distributor comprises at least one vessel with an upstream portion and an adjacent down-stream portion, wherein the upstream portion of the vessel comprises a first lateral end comprising an inlet and an opposite second lateral end being connected with the downstream portion, wherein the downstream portion of the vessel comprises a first lateral end and an opposite second lateral end with the first lateral end being connected with the second lateral end of the upstream portion, and wherein the downstream portion of the vessel comprises a hollow double-plate assembly, wherein the hollow double-plate assembly comprises an upper plate and a lower plate being arranged on top of each other, but spaced apart so that a void cham-ber is defined therebetween, wherein each of both plates comprises a plurality of openings, wherein each opening of the upper plate is surrounded by a wall extend-ing through the void chamber and surrounding an opening of the lower plate so as to form a plurality of channels being fluid-tightly separated from the hollow space being defined in the void chamber between the channels, wherein the hollow space is connected with an inlet for heat medium and with an outlet for heat medi-um.

A waste processing apparatus is disclosed which includes a waste processing vessel for holding waste and treatment fluid during processing, and a fluid delivery system for delivering a treatment fluid to the waste processing vessel. The fluid delivery system comprises a settling vessel located upstream of the waste processing vessel, the settling vessel defining an internal volume configured to retain a treatment fluid, a first fluid transfer means arranged and configured to transfer the treatment fluid from a fluid reservoir to the settling vessel; and a second fluid transfer means arranged and configured to deliver treatment fluid from the settling vessel to the waste processing vessel. The fluid delivery system is configured such that treatment fluid is retained in the settling vessel for a period of time prior to delivery to the waste processing vessel.

A multi-functional slurry processing system (“VARCOR”) and associated methods is disclosed. The present examples provide a multi-functional slurry processing system incorporating systems and methods for separating liquid and solid components in slurries. In particular the systems and methods described herein produce clean water, dried solids, and potential concentration of desirable constituents with a boiling point lower than water. At least one example of the multi-functional slurry processing system provides a self-contained processing facility configured to efficiently convert high water-content slurries into its constituent solid and liquid fractions and subsequently generating and collecting clean water and concentrating desirable constituents with a boiling point lower than water. The multi-functional slurry processing system advantageously applies thermodynamic principles in a system which may include various combinations of a preheater, a degassing unit, a dryer, a steam filter, a compressor, a concentrating tower, and a condensation unit.

The present invention provides an integrated multiphase biocatalytic reactor and separator system (1), comprising, an upflow reaction section (2), a separation section (3), and a recycle flow section (4), wherein: the upflow reaction section (2) comprises a gas phase inlet (12), arranged to introduce a gas phase (G) for lifting a reactor flow (C) comprising a first and a second phase liquid; the separation section includes a first separation zone (31) configured to degas an effluent flow from the upflow section, and a second separation zone (32), i.e. a liquid-liquid phase separator, configured to separate the degassed effluent in a lower liquid phase (LP) and an upper liquid phase (UP), said second separation zone further comprising an outlet (15) for collecting the upper liquid phase and an outlet for recirculating the lower liquid phase back to the upflow reaction section via the recycle flow section (4).

The invention belongs to the technical field of oil field sewage treatment, and particularly relates to an oil field three-phase separator. The oil field three-phase separator comprises a separator main body, a first cavity, a second cavity and a third cavity are sequentially arranged in the separator main body from left to right, a rectification emulsion breaker is arranged between the first cavity and the second cavity, and a partition plate is arranged between the second cavity and the third cavity; the cyclone separator is arranged on the separator main body; and the cyclone separator is communicated with the first cavity of the separator main body.

A heatable distributor includes a vessel with an upstream portion and an adjacent downstream portion, the upstream portion includes a first lateral end with an inlet and a second lateral end connected with the downstream portion. the downstream portion includes a first lateral end and a second lateral end, the first lateral end connected with the second lateral end of the upstream portion, and the downstream portion includes a hollow double-plate assembly including an upper plate and a lower plate spaced apart so that a void chamber is defined therebetween. Each plate includes openings, each opening of the upper plate is surrounded by a wall extending through the void chamber and surrounding an opening of the lower plate to form channels being fluid-tightly separated from the hollow space and, the hollow space is connected with an inlet for a heat medium and with an outlet for the heat medium.

The present invention relates to a heatable distributor, in particular a devolatilization apparatus for devolatilizing compositions comprising volatile components, such as for devolatilizing solid or liquid polymer compositions comprising unreacted monomers, solvents and / or by-products, the heatable distributor includes at least one tank having an upstream portion and an adjacent downstream portion, where the upstream portion of the tank includes a first side end and an opposite second side end connected to the downstream portion, the first side end including an inlet, where the downstream portion of the tank includes a first side end and an opposite second side end, the first side end is connected to the second side end of the upstream portion, and wherein the downstream portion of the tank comprises a hollow double-plate assembly wherein the hollow double-plate assembly comprises an upper plate and a lower plate which are arranged one above the other but spaced apart such that a void chamber is defined therebetween wherein each of the two plates comprises a plurality of openings, wherein each opening of the upper plate is surrounded by a wall extending through the void chamber and surrounding the opening of the lower plate so as to form a plurality of channels which are fluid-tightly separated from a hollow space defined in the void chamber between the channels, and wherein the hollow space is connected to an inlet for the thermal medium and an outlet for the thermal medium.

The present invention relates to a method for producing lysine, comprising a step of culturing a microorganism to prepare a fermentation broth containing lysine; and a step of removing carbon dioxide from the fermentation broth containing lysine using a carbon dioxide stripping tower.

The present invention relates to the field of lithium battery diaphragm defoaming, and in particular to a lithium battery diaphragm coating defoaming device and a defoaming method. A lithium battery diaphragm coating defoaming device and a defoaming method, comprising a bracket, the bracket being fixedly connected to an outer shell, the outer shell being fixedly connected to a feed pipe, a suction and pressure pipe, and a discharge pipe, a first servo motor and a second servo motor being fixedly connected to the inner part of the outer shell, a separation component for separating coating clots and bubbles being provided at the inner bottom of the outer shell, a lifting component for lifting the lithium battery diaphragm coating being provided inside the outer shell, an extrusion component for squeezing bubbles and clots in the coating being provided inside the outer shell, and a cleaning component for cleaning the coating accumulation on the inner wall of the outer shell being provided on the lifting component. The inner shell is rotated to separate bubbles and clots through centrifugation, and the centrifugal force drives the friction block to decompose and quickly dissolve the clots through friction, while the bubble coating is lifted and defoamed after centrifugal counteraction and vacuum environment, thereby ensuring uniform coating of the lithium battery diaphragm.

The invention discloses a gas-liquid separation system and method, an inlet mass flow meter is arranged at an inlet of a gas-liquid separator cylinder, an electronic back pressure valve and a mass flow meter are arranged on an overflow pipe of the gas-liquid separator cylinder, and a double-ring conducting probe and an electronic back pressure valve are arranged on an underflow pipe of the gas-liquid separator cylinder; a differential pressure sensor is arranged between the underflow pipe and the overflow pipe; the upper computer unit is used for adjusting the height of a vortex stabilizing plate in the gas-liquid separator and the back pressure difference between an overflow port and an underflow port through PID feedback, gas-liquid phase interface distribution in the separator can be adjusted to a certain degree, real-time adjustment can be carried out according to different inlet working conditions, stability and automatic control of a flow field in the gas-liquid separator are achieved, and the gas-liquid separator is suitable for large-scale production. And meanwhile, the requirement of signal far-end transmission is met. The system is reasonable in structural design and flexible in application scene, the problem that the efficient working condition interval of a traditional gas-liquid separator is narrow is effectively solved, and the efficient working condition interval of the gas-liquid separator is widened.

The invention relates to a two-stage oil-gas separation dynamic pressure type oil-gas separator which comprises a wake flow separator used for first-time gas-oil separation and a dynamic pressure type oil-gas separator used for second-time gas-oil separation, and the wake flow separator is arranged on an oil return pipe corresponding to an oil return opening of the dynamic pressure type oil-gas separator; the invention further discloses a secondary oil-gas separation method of the dynamic pressure type oil-gas separator for two-stage oil-gas separation. The secondary oil-gas separation method specifically comprises a two-stage oil-gas separation process and a wake flow separator oil-gas separation process. Aiming at the problems that a dynamic pressure type oil-gas separator used by a small engine is not high in efficiency and cannot guarantee effective separation of lubricating oil and air, the invention provides the oil-gas separator and the separation method which are subjected to two-time oil-gas separation, so that the separation efficiency of the oil-gas separator is effectively improved, and the oil-gas separator has a relatively good engineering application value.

A geothermal plant (1600, 1700, 1800, 2000), for extracting energy from a geothermal reservoir (1230) located below the ocean bottom, includes a floating platform (1202); a riser (1240) that extends from a well (1208) drilled into the geothermal reservoir (1230), to the floating platform (1202); an electrical pump (1260) having a mechanical actuation part (1264) located in a bore of the riser (1240), and an electronic part (1266) located outside the riser, wherein the electrical pump (1260) is configured to pump a geothermal liquid (1226) from the geothermal reservoir (1230) to the floating platform (1202); and a power plant (1210) located on the floating platform (1202) and configured to use a steam (1222) produced by the geothermal liquid (1226) to generate electrical power. The electrical pump (1260) is placed at a depth of the riser (1240) where the geothermal liquid (1226) is in a single-phase.