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| 20120245395 | Reduced Energy Alcohol Separation Process Having Water Removal - The present invention relates to the recovery of alcohols, in particular ethanol, from a crude ethanol product obtained from the hydrogenation of acetic acid using a reduced energy process. The crude ethanol product may be fed to a distillation column in which a substantial portion of the water is removed with the acetic acid in the residue. Additional water may be removed by using a pressure swing adsorption unit, molecular sieve, and/or membrane. Ethanol extraction may also be used to reduce the ethanol concentration in the recycle streams. | 09-27-2012 |
| 20120245396 | Recovering Ethanol Sidedraw By Separating Crude Product From Hydrogenation Process - A process for producing ethanol is disclosed, comprising the steps of hydrogenating acetic acid in a reactor in the presence of a catalyst to form a crude ethanol product, separating at least a portion of the crude ethanol product in a column into a first distillate comprising ethanol and a first residue comprising acetic acid and water, wherein a substantial portion of the water in the crude ethanol product that is fed to the column is removed in the first residue, and separating a portion of the ethanol mixture stream to the second distillation column to yield an ethanol product sidedraw, second residue comprising water and a second distillate comprising ethyl acetate. The water content of the ethanol product sidedraw may be further reduced to yield a stream having reduced water content. | 09-27-2012 |
| 20120277491 | REDUCING ETHYL ACETATE CONCENTRATION IN RECYCLE STREAMS FOR ETHANOL PRODUCTION PROCESSES - Recycle streams in an ethanol production process are hydrolyzed to reduce ethyl acetate concentration. In the process, acetic acid is hydrogenated to form a crude ethanol product, which undergoes a separation or purification process. Ethyl acetate is formed as a byproduct of the hydrogenation of acetic acid. The hydrolysis of recycle steams from the separation process can reduce the concentration of ethyl acetate, converting some or all of the ethyl acetate to acetic acid and ethanol. | 11-01-2012 |
| 20120277493 | Process to Recover Alcohol with Secondary Reactors for Hydrolysis of Acetal - A process for recovering ethanol obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in a column to produce a distillate stream comprising acetaldehyde and ethyl acetate and a residue stream comprising ethanol, acetic acid and water. Acetal byproduct can be reduced or removed through configurations of hydrolysis secondary reactors. The ethanol product is recovered from the residue stream. | 11-01-2012 |
| 20120277494 | Process to Reduce Ethanol Recycled to Hydrogenation Reactor - The present invention is directed to processes for recovering ethanol obtained from the hydrogenation of acetic acid. Acetic acid is hydrogenated in the presence of a catalyst in a hydrogenation reactor to form a crude ethanol product. The crude ethanol product is separated in one or more columns to recover ethanol. In some embodiments, less than 10 wt. % ethanol is recycled to the hydrogenation reactor. | 11-01-2012 |
| 20120277495 | Process For Controlling A Reboiler During Alcohol Recovery and Reduced Ester Formation - The present invention is related to processes for the separation of ethanol from a crude ethanol product obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in one or more columns. A reboiler is used following one or more of the columns for reducing ester formation. | 11-01-2012 |
| 20120277496 | Process for Producing Ethanol and Reducing Acetic Acid Concentration - A process for producing ethanol and, in particular, to a process for reducing the concentration of acetic acid in a crude ethanol product by esterifying unreacted acetic acid with an alcohol. | 11-01-2012 |
| 20120277497 | Process to Recover Alcohol with Reduced Water From Overhead of Acid Column - A process for recovering ethanol obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in a column to produce a distillate stream comprising acetaldehyde and ethyl acetate and a residue stream comprising ethanol, acetic acid, ethyl acetate and water. The ethanol product is recovered from the residue stream. | 11-01-2012 |
| 20130109891 | Process to Recover Alcohol with Secondary Reactors for Esterification of Acid | 05-02-2013 |
| 20130131400 | Hydrogenating Acetic Acid to Produce Ethyl Acetate and Reducing Ethyl Acetate to Ethanol - Disclosed herein are processes for alcohol production by reducing an ethyl acetate produced by hydrogenating acetic acid in the presence of a suitable catalyst. The ethyl acetate is reduced with hydrogen in the presence of a catalyst to obtain a crude reaction mixture comprising the alcohol, in particular ethanol, which may be separated from the crude reaction mixture. Thus, ethanol may be produced from acetic acid through an ethyl acetate intermediate without an esterification step. This may reduce the recycle of ethanol in the hydrogenolysis process and improve ethanol productivity. | 05-23-2013 |
| 20130158297 | ESTERIFYING AN ETHANOL AND ACETIC ACID MIXTURE TO PRODUCE AN ESTER FEED FOR HYDROGENOLYSIS - Disclosed herein are processes for alcohol production by hydrogenating acetic acid to obtain a mixture of ethanol and acetic acid, esterifying the mixture to produce an esterification product and reducing the esterification product. The mixture may provide a sufficient amount of ethanol and acetic acid for esterification and reduces the need for additional acetic acid and/or ethanol. This may reduce the recycle of ethanol in the hydrogenolysis process and improve ethanol productivity. | 06-20-2013 |
| 20130158302 | Phasing Reactor Product from Hydrogenating Acetic Acid Into Ethyl Acetate Feed to Produce Ethanol - Disclosed herein are processes for alcohol production by reducing ethyl acetate produced by hydrogenating acetic acid in the presence of a suitable catalyst. The product of the acetic acid hydrogenation is fed directly to a decanter to separate the hydrogenation product into an aqueous phase comprising water and ethanol and an organic phase comprising ethyl acetate. The organic phase is reduced with hydrogen in the presence of a catalyst to obtain a crude reaction mixture comprising the alcohol, in particular ethanol, which may be separated from the crude reaction mixture. Thus, ethanol may be produced from acetic acid through an ethyl acetate intermediate without an esterification step. This may reduce the recycle of ethanol in the hydrogenolysis process and improve ethanol productivity. | 06-20-2013 |
| 20130184500 | Process for Acetal Removal In the Purification of a Crude Ethanol Product - Recovery of ethanol from a crude ethanol product obtained from the hydrogenation of acetic acid. Separation and purification processes of the crude ethanol products are employed to allow recovery of ethanol and hydrolyze acetal impurities by the addition of an acid stream. | 07-18-2013 |
| 20130245333 | Ethanol Manufacturing Process Over Catalyst Having Improved Radial Crush Strength - Acetic acid is hydrogenation in the presence of a catalyst comprising one or more active metals on a silica support, wherein the catalyst has a radial crush strength of at least 4 N/mm. The one or more active metals may include cobalt, copper, gold, iron, nickel, palladium, platinum, iridium, osmium, rhenium, rhodium, ruthenium, tin, zinc, lanthanum, cerium, manganese, chromium, vanadium, molybdenum and mixtures thereof. Radial crush strength may be improved by steam treating the catalyst support prior to the loading of the one or more active metals. | 09-19-2013 |
| 20140142351 | Combined Column for Separating Products of Different Hydrogenation Reactors - Recovery of ethanol from a crude product comprising ethyl acetate obtained from the hydrogenation of acetic acid. The crude product is separated to form an organic stream that may be subjected to hydrogenolysis to form ethanol. The organic phase may comprise ethyl acetate is reacted via hydrogenolysis form ethanol that may be directly or indirectly fed to the separation zone or the hydrogenation reactor. | 05-22-2014 |
| 20150024928 | Ethanol Manufacturing Process Over Catalyst Having Improved Radial Crush Strength - Acetic acid is hydrogenation in the presence of a catalyst comprising one or more active metals on a silica support, wherein the catalyst has a radial crush strength of at least 4 N/mm. The one or more active metals may include cobalt, copper, gold, iron, nickel, palladium, platinum, iridium, osmium, rhenium, rhodium, ruthenium, tin, zinc, lanthanum, cerium, manganese, chromium, vanadium, molybdenum and mixtures thereof. Radial crush strength may be improved by steam treating the catalyst support prior to the loading of the one or more active metals. | 01-22-2015 |
| 20150099905 | Process to Recover Alcohol with Reduced Water From Overhead of Acid Column - A process for recovering ethanol obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in a column to produce a distillate stream comprising acetaldehyde and ethyl acetate and a residue stream comprising ethanol, acetic acid, ethyl acetate and water. The ethanol product is recovered from the residue stream. | 04-09-2015 |
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| 20120191735 | SESSION TABLE FRAMEWORK - In accordance with embodiments disclosed herein, there are provided methods, systems, and apparatuses for implementing a session table framework including, for example, receiving a request at a host organization from a client device, in which such a request specifies an application available via the host organization; generating a user session unique to the client device in a memory of the host organization; creating a user session data table within the user session; processing the request via the application specified by the request on behalf of the client device; updating the user session data table based on the processing of the request; and transmitting a response to the client device responsive to the request. | 07-26-2012 |
| 20120191865 | SESSION TABLE FRAMEWORK - In accordance with embodiments disclosed herein, there are provided methods, systems, and apparatuses for implementing a session table framework including, for example, receiving a configuration request at a host organization from a client device; generating, via a configurator engine of the host organization, a configuration model having metadata therein; generating a user session unique to the client device in a memory of the host organization; creating a user session data table within the user session of the memory based on the metadata of the configuration model; populating data into the user session data table based on the metadata of the configuration model; generating a renderable User Interface (UI) based on the metadata of the configuration model and based further on the data in the user session data table; and transmitting the renderable UI to the client device for display, responsive to receiving the configuration request. | 07-26-2012 |
| 20140143285 | SESSION TABLE FRAMEWORK - In accordance with embodiments disclosed herein, there are provided methods, systems, and apparatuses for implementing a session table framework including, for example, receiving a request at a host organization from a client device, in which such a request specifies an application available via the host organization; generating a user session unique to the client device in a memory of the host organization; creating a user session data table within the user session; processing the request via the application specified by the request on behalf of the client device; updating the user session data table based on the processing of the request; and transmitting a response to the client device responsive to the request. | 05-22-2014 |
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| 20090307034 | ENERGY INFORMATION MANAGEMENT SYSTEM - An energy information management system and a computer-implemented method of managing energy information are disclosed. The computer-implemented method may include receiving energy use data based upon the energy consumption of one or more facilities, associating the energy use data with one or more facility types based upon characteristics of the one or more facilities to which the energy use data is related, and storing the energy use data in a database. Each facility type may be determined based upon at least one of an owner, location, size, age, use, operating schedule, lighting, water use, and heating, ventilation, and air conditioning equipment of the facility to which the energy use data is related. The energy information management system may include one or more sources of energy use data which generate data signals, a server, and a browser-enabled user device. | 12-10-2009 |
| 20090307573 | ENERGY MANAGEMENT SYSTEM - An energy management system and a computer-implemented method of managing energy consumption are disclosed. The computer-implemented method may include receiving one or more input signals which represent the real-time energy consumption of a facility, evaluating data obtained from the one or more input signals according to a set of energy operating rules, and generating output signals which cause a user to be alerted to the energy consumption of the facility. In some embodiments, evaluating data obtained from the one or more input signals according to a set of energy operating rules may include comparing the obtained data to predetermined or adaptive ranges or thresholds. The ranges or thresholds may be based upon at least one of an operational schedule of the facility, physical characteristics of the facility, energy-sensitive variables, customer-imposed targets, and energy supplier demand reduction requests. The system and method may detect anomalous energy use and send an alert message to a user or a browser-enabled user device. | 12-10-2009 |
| 20140114489 | SUSTAINABLE ENERGY EFFICIENCY MANAGEMENT SYSTEM - Illustrative embodiments of a sustainable energy management system (SEEMS) are disclosed. Embodiments of the SEEMS may illustratively include a sustainable energy efficiency hardware platform, a local sustainable energy efficiency software platform, a hosted sustainable energy efficiency software platform, and a sustainable energy efficiency business process. The SEEMS may generate graphical energy efficiency reports, graphical budget impact reports, and graphical energy summary reports, among many other outputs. | 04-24-2014 |
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| 20120164048 | PROCESS FOR SELECTIVE REMOVAL OF ACETYLENES FROM GASEOUS STREAMS - The present discloses a process and catalyst therefor to selectively remove acetylenes from gaseous streams in the vapor phase. The process is particularly suitable for high yield recovery of olefinic hydrocarbons from gaseous streams in refinery processes. | 06-28-2012 |
| 20130158289 | PRODUCTION OF DIACETOXYETHYLENE BY DIRECT ACETOXYLATION - In one embodiment, the invention is to a process for producing a vinyl acetate composition by contacting a vinyl acetate stream with acetic acid, ethylene, and oxygen to form a reaction mixture and reacting the reaction mixture in a reactor under conditions effective to form a crude vinyl acetate composition comprising vinyl acetate, water, acetic acid and at least 0.1 wt % diacetoxyethylene. | 06-20-2013 |
| 20140024766 | COPOLYMERS OF 1,2-DIACETOXYETHYLENE AND VINYL ACETATE, PROCESS OF MAKING THE COPOLYMERS AND PROCESS OF MAKING A COPOLYMERIZED POLYVINYL ALCOHOL - In one embodiment, the invention is to a vinyl acetate/diacetoxyethylene copolymer, processes of making the copolymer and processes of hydrolyzing said copolymer to form a copolymerized polyvinyl alcohol. | 01-23-2014 |
| 20150018589 | Manufacture of Butadiene from Ethylene - A method of producing butadiene includes: (1) dimerizing ethylene to butene followed by (2) oxidatively dehydrogenating the butene to butadiene and (3) recovering the butadiene by (i) absorbing the product with a hydrocarbon absorber oil and (ii) stripping a crude product stream from the absorber oil. The absorber oil is selected so as to be effective to sequester ethylene dimerization-derived impurities from the system. | 01-15-2015 |
| 20150073184 | Controllability Oxidative Dehydrogenation Process for Producing Butadiene - Butadiene is made from a butene rich feed, passing a superheated butene rich feed including superheated steam and oxygen at a temperature of at least about 343° C. (650° F.) over a catalyst bed having a depth of over about 69 cm (27 inches) of granules of ferritic oxidative dehydrogenation catalyst. Inlet conditions being controlled such that the oxidative dehydrogenation reactions initially occur in the lower most layers of catalyst. Process control includes monitoring the temperature throughout the bed and increasing the inlet temperature in response to a drop in the temperature in the active layer, when the active layer of oxidative dehydrogenation catalyst begins to become deactivated so that the reaction zone moves upwardly in the oxidative dehydrogenation bed. | 03-12-2015 |
| 20150080627 | Low Emissions Oxidative Dehydrogenation Process for Producing Butadiene - Butadiene is formed by dehydrogenation of butenes which are mixed with steam and oxygen then converted to butadiene by oxidative dehydrogenation over a ferritic oxide catalyst, wherein the sensible heat in the oxidative dehydrogenation reaction product is utilized along with heat produced by thermal oxidation of low value volatile products formed to reduce energy requirements and CO | 03-19-2015 |
| 20150315107 | Process for Selective Removal of Acetylenes from Gaseous Streams - The present discloses a process and catalyst therefor to selectively remove acetylenes from gaseous streams in the vapor phase. The process is particularly suitable for high yield recovery of olefinic hydrocarbons from gaseous streams in refinery processes. | 11-05-2015 |
| 20160002126 | Oxidative Dehydrogenation Process With Hydrocarbon Moderator Gas and Reduced Nitrogen Feed - Oxidative dehydrogenation includes: (a) providing a gaseous feed stream to a catalytic reactor, the feed stream comprising a dehydrogenation reactant, oxygen, superheated steam, hydrocarbon moderator gas and optionally nitrogen, wherein the molar ratio of moderator gas to oxygen in feed stream is typically from 4:1 to 1:1 and the molar ratio of oxygen to nitrogen in the feed stream is at least 2; (b) oxidatively dehydrogenating the reactant in the reactor to provide a dehydrogenated product enriched effluent product stream; and (c) recovering dehydrogenated product from the effluent product stream. One preferred embodiment is a process for making butadiene including dimerizing ethylene to n-butene in a homogeneous reaction medium to provide a hydrocarbonaceous n-butene rich feed stream and oxidatively dehydrogenating the n-butene so formed. | 01-07-2016 |
| 20160023963 | Multi-Stage Oxidative Dehydrogenation Process with Inter-Stage Cooling - A method of oxidatively dehydrogenating a dehydrogenation reactant includes providing a first gaseous feed stream to a first adiabatic, catalytic reaction zone with less than a stoichiometric amount of oxygen and superheated steam, oxidatively dehydrogenating dehydrogenation reactant in said first adiabatic, catalytic reaction zone and subsequently cooling the effluent, adding additional oxygen and reacting the effluent stream in at least one subsequent adiabatic reaction zone. The deydrogenation system enables higher conversion and yield per pass and in some cases greatly reduces steam usage and energy costs. In a preferred integrated process, ethylene is converted to n-butene which is then oxidatively dehydrogenated to butadiene. | 01-28-2016 |
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| 20140137067 | FILTER DESIGN TOOL - A method according to an embodiment of a filter design tool is provided and includes receiving filter parameters for an analog filter through a user interface, where the filter parameters include an optimization parameter related to an application requirement of the analog filter, optimizing the filter for the optimization parameter, calculating a design output based on the optimized filter, and displaying the design output on the user interface. The method can further include receiving viewing parameters that specify the design output to be displayed. In various embodiments, the user interface includes an input area, a viewing area and a window area in one or more pages, where the input area is contiguous to the viewing area in at least one page. The filter parameters can be entered in the input area and the design output is calculated and displayed in the contiguous viewing area substantially immediately. | 05-15-2014 |
| 20140137068 | FILTER DESIGN TOOL - A method according to an embodiment of a filter design tool is provided and includes receiving filter parameters for an analog filter through a user interface, where the filter parameters include an optimization parameter related to an application requirement of the analog filter, optimizing the filter for the optimization parameter, calculating a design output based on the optimized filter, and displaying the design output on the user interface. The method can further include receiving viewing parameters that specify the design output to be displayed. In various embodiments, the user interface includes an input area, a viewing area and a window area in one or more pages, where the input area is contiguous to the viewing area in at least one page. The filter parameters can be entered in the input area and the design output is calculated and displayed in the contiguous viewing area substantially immediately. | 05-15-2014 |
| 20140137069 | FILTER DESIGN TOOL - A method according to an embodiment of a filter design tool is provided and includes receiving filter parameters for an analog filter through a user interface, where the filter parameters include an optimization parameter related to an application requirement of the analog filter, optimizing the filter for the optimization parameter, calculating a design output based on the optimized filter, and displaying the design output on the user interface. The method can further include receiving viewing parameters that specify the design output to be displayed. In various embodiments, the user interface includes an input area, a viewing area and a window area in one or more pages, where the input area is contiguous to the viewing area in at least one page. The filter parameters can be entered in the input area and the design output is calculated and displayed in the contiguous viewing area substantially immediately. | 05-15-2014 |
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| 20120318136 | HOT GAS FILTRATION MEDIA AND FILTERS - A nonwoven felt for hot gas filtration. The fibers have a polyarylene sulfide (PAS) component that contains a zinc compound. In one embodiment, the PAS comprises at least one zinc(II) salt of an organic carboxylic acid. Also a method for filtering hot gases employing a bag made from a PAS component that contains a zinc or a zinc based additive. | 12-20-2012 |
| 20130009333 | PROCESS FOR MAKING NONWOVEN WEBS - A nonwoven web comprising bicomponent fibers. The fibers have continuous phases each of a first polyarylene sulfide (PAS) component and a polymer component. The polymer component may also be a second polyarylene sulfide. The first polyarylene sulfide component contains a tin or a zinc additive or both, and the first polyarylene sulfide component of any given fiber is at least partially exposed to the external surface of that fiber. | 01-10-2013 |
| 20130012671 | CURE ACCELERATION OF POLYMERIC STRUCTURES - A method for accelerating the curing of a polyarylene sulfide. The polyarylene sulfide is blended with a cure accelerator to form a mixture where the weight percentage of accelerator is between 0.2% and 15.0% of the total weight of the blend. The mixture is cured at 320° C. or above for at least 20 minutes. The cure accelerator is a compound selected from the group consisting of ionomers, hindered phenols, polyhydric alcohols, polycarboxylates, and mixtures of the foregoing. | 01-10-2013 |
| 20140087117 | POLYPHENYLENE SULFIDE COMPOSITIONS - Provided are polyphenylene sulfide compositions having improved thermo-oxidative stability, methods for obtaining them, and articles comprising the compositions. The compositions comprise polyphenylene sulfide and a bismuth additive. The bismuth additive comprises a bismuth halide, an inorganic bismuth salt, a bismuth carboxylate, an oxide comprising bismuth and a transition metal, bismuth metal, or a mixture thereof. Optionally, the compositions further comprise at least one zinc(II) compound. | 03-27-2014 |
| 20140097134 | SOLUTION PHASE PROCESSING OF POLYARYLENE SULFIDE - Provided are methods for obtaining modified polyarylene sulfide compositions having improved thermal and thermo-oxidative stability, the compositions so obtained, and articles comprising the compositions. The method comprises the steps of contacting, in the presence of a suitable solvent, a polyarylene sulfide with at least one reducing agent and at least base to form a first mixture. The reducing agent comprises zinc(0), tin(0), tin(II), bismuth (0), bismuth(III), or a combination thereof. The first mixture is heated to form a second mixture in which the polyarylene sulfide is dissolved. The polyarylene sulfide is then precipitated to obtain a modified polyarylene sulfide. | 04-10-2014 |
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| 20090272380 | EXHAUST PORT ASSEMBLY FOR A PRESSURE SUPPORT SYSTEM - An exhaust port assembly comprising a conduit carries a flow of gas. A vent assembly having a fixed exhaust area is provided on the conduit for venting a flow of exhaust gas from within the conduit to ambient atmosphere. The vent assembly is configured so as to minimize noise associated with the flow of exhaust gas passing to atmosphere, diffuse the flow of exhaust gas passing to ambient atmosphere over a relatively large area, and minimize the area occupied by the venting assembly on the conduit. | 11-05-2009 |
| 20100186743 | METHOD AND APPARATUS FOR TREATING CHEYNE-STOKES RESPIRATION - A system and method for delivering a flow of breathing gas to an airway of a patient. The system monitors a characteristic that varies based on variations of the flow of the breathing gas and determines a Target Flow for the gas to be delivered to the patient based on the monitored characteristic. The Target Flow is set to a level sufficient to treat Cheyne-Stokes respiration or a sleep disordered breathing event. The system also alters the Target Flow based on a determination that the patient is experiencing a sleep disordered breathing event. The system further determines a pressure relief component and controls the flow of gas delivered to the patient based on the Target Flow and the pressure relief component. | 07-29-2010 |
| 20110197883 | PORTING BLOCK FOR A MEDICAL VENTILATOR - A ventilator that is small, lightweight, and portable, yet capable of being quickly adapted to operate in a plurality of different modes and configurations to deliver a variety of therapies to a patent. A porting system having a plurality of sensors structured to monitor a number of parameters with respect to the flow of gas, and a number of porting blocks is used to reconfigure the ventilator so that it operates as a single-limb or dual limb ventilator. In the single-limb configuration, an active or passive exhaust assembly can be provided proximate to the patient. The ventilator is capable of operate in a volume or pressure support mode, even in a single-limb configuration. In addition, a power control mechanism controls the supply of power to the ventilator from an AC power source, a lead acid battery, an internal rechargeable battery pack, and a detachable battery pack. | 08-18-2011 |
| 20110197884 | VOLUME CONTROL IN A MEDICAL VENTILATOR - A ventilator that is small, lightweight, and portable, yet capable of being quickly adapted to operate in a plurality of different modes and configurations to deliver a variety of therapies to a patient. A porting system having a plurality of sensors structured to monitor a number of parameters with respect to the flow of gas, and a number of porting blocks is used to reconfigure the ventilator so that it operates as a single-limb or dual limb ventilator. In the single-limb configuration, an active or passive exhaust assembly can be provided proximate to the patient. The ventilator is capable of operate in a volume or pressure support mode, even in a single-limb configuration. In addition, a power control mechanism controls the supply of power to the ventilator from an AC power source, a lead acid battery, an internal rechargeable battery pack, and a detachable battery pack. | 08-18-2011 |
| 20110209706 | VENTILATOR WITH LIMP MODE - A method of operating a ventilator that includes steps of (a) providing a specified ventilation therapy to a patient through a ventilator according to a specification; (b) determining and storing a backup parameter relating to the operation of the ventilator or the breathing of the patient during the step of providing the specified ventilation therapy; (c) determining that an alarm condition exists that indicates a problem with the ventilator that would prevent the ventilator from providing the specified ventilation therapy to the patient according to the specification; and (d) responsive to determining that the alarm condition exists, providing backup ventilation therapy to the patient through the ventilator that is based at least partially on the stored backup parameter. Also, a ventilator that is adapted to perform the method just described. | 09-01-2011 |
| 20120152252 | AUTO-TITRATION BI-LEVEL PRESSURE SUPPORT SYSTEM AND METHOD OF USING SAME - A bi-level pressure support system and method of treating disordered breathing that optimizes the pressure delivered to the patient during inspiration and expiration to treat the disordered breathing while minimizing the delivered pressure for patient comfort. The pressure generating system generates a flow of breathing gas at an inspiratory positive airway pressure (IPAP) during inspiration and at an expiratory positive airway pressure (EPAP) during expirations. A controller monitor at least one of the following conditions: (1) snoring, (2) apneas, (3) hypopneas, or (4) a big leak in the pressure support system and adjusts the IPAP and the EPAP based on the occurrence of any one of these conditions. | 06-21-2012 |
| 20120255552 | METHOD AND APPARATUS FOR TREATING CHEYNE-STOKES RESPIRATION - A system and method for delivering a flow of breathing gas to an airway of a patient. The system monitors a characteristic that varies based on variations of the flow of the breathing gas and determines a Target Flow for the gas to be delivered to the patient based on the monitored characteristic. The Target Flow is set to a level sufficient to treat Cheyne-Stokes respiration or a sleep disordered breathing event. The system also alters the Target Flow based on a determination that the patient is experiencing a sleep disordered breathing event. The system further determines a pressure relief component and controls the flow of gas delivered to the patient based on the Target Flow and the pressure relief component. | 10-11-2012 |
| 20140182589 | METHOD AND APPARATUS FOR TREATING CHEYNE-STOKES RESPIRATION - A system and method for delivering a flow of breathing gas to an airway of a patient. The system monitors a characteristic that varies based on variations of the flow of the breathing gas and determines a Target Flow for the gas to be delivered to the patient based on the monitored characteristic. The Target Flow is set to a level sufficient to treat Cheyne-Stokes respiration or a sleep disordered breathing event. The system also alters the Target Flow based on a determination that the patient is experiencing a sleep disordered breathing event. The system further determines a pressure relief component and controls the flow of gas delivered to the patient based on the Target Flow and the pressure relief component. | 07-03-2014 |
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| 20110226248 | AUTOMATIC RISE TIME ADJUSTMENT - A method of providing pressure support to a patient that includes determining a measure associated with an inspiratory time of the patient during therapy, delivering a flow of breathing gas to the patient at an inspiratory positive airway pressure (IPAP) level during at least a portion of an inspiratory phase of the patient, delivering the flow of breathing gas to the patient at an expiratory positive airway pressure (EPAP) level that is less than the IPAP level during at least a portion of an expiratory phase of the patient, and automatically setting a rise time associated with a transition from the EPAP level to the IPAP level based on the measure associated with the inspiratory time of the patient. Also provided is a pressure support system adapted to perform the method. | 09-22-2011 |
| 20140076317 | PULSE OXIMETRY IN RESPIRATORY THERAPY PATIENT INTERFACE - Provided are systems and methods for utilizing blood oxygenation information with respiratory therapy. These systems and methods may provide respiratory therapy to a patient ( | 03-20-2014 |
| 20150136134 | COUGH ASSISTANCE AND MEASUREMENT SYSTEM AND METHOD - Systems and methods are configured to inexsufflate a subject and provide cough-by-cough feedback during treatment and/or therapy of the subject. Through sensors that are included in the systems, various gas and/or respiratory parameters maybe measured and/or determined in real-time, such as, for example, peak cough flow and/or inspiratory tidal volume. | 05-21-2015 |
| 20150182721 | HUMIDIFIER WITH BACK-FLOW PREVENTION VALVE - A humidifier for use with a pressure support system. The humidifier includes a body having an inlet, a fluid holding chamber, and an outlet. The inlet is positioned upstream and in fluid communication with the fluid holding chamber. The outlet is positioned downstream of and in fluid communication with the fluid holding chamber. A back-flow preventing valve is positioned upstream of the fluid chamber. The back-flow preventing valve is movable between an open position, in which the inlet is unblocked, and a closed position in which the inlet is blocked. In the closed position, the back-flow preventing valve prevents fluid, fluid vapor, or both from entering the pressure support via the inlet to the humidifier. | 07-02-2015 |
