55 results about "Vapor quality" patented technology

A gas turbine intercooler operates to heat a predetermined organic fluid via heat generated by the gas turbine. The heated organic fluid remains in a partially evaporated or non-evaporated liquid phase to provide a heated organic fluid that reaches a state of saturation with a vapor quality less than unity. An expansion machine expands the heated organic fluid via a Tri-Lateral Flash cycle to increase the vapor quality and generate electrical power therefrom.

Determination of steam quality by passing one or more laser beams through steam in a steam chamber and directly determining a total number of vapor molecules and a total number of water molecules based on absorption of radiation in the one or more laser beams by the water vapor phase and the liquid water phase in the steam. Specific volumes of water vapor phase and liquid water phase in the steam using the total numbers of water vapor and liquid water molecules are determined and the quality of the steam is calculated based on the specific volumes of the water vapor phase and the liquid water phase in steam. One embodiment comprises a narrow linewidth laser for measuring steam quality and another embodiment comprises multiple broadband lasers for measuring steam quality.

The invention relates to thermally stimulated oil recovery in horizontal wells, namely to the methods for estimation of Steam Assisted Gravity Drainage (SAGD) process characteristics. Method for estimation of SAGD process characteristics is characterized by the steps of measuring temperature along the injection well, measuring steam quality and injection rate at the inlet of the injection well, estimating the pressure distribution profile by using the data obtained, estimating steam injection profile by using the obtained pressure profile and injection rate combined with ID injection well model for pressure losses in the wellbore and heat exchange between injection well tubing and annulus. The obtained steam injection profile is used as an input parameter for a set of 2D cross-sectional analytical SAGD models taking into account reservoir and overburden formation properties impact on production parameters and SAGD characteristics. SAGD process characteristics are estimated on the basis of energy conservation law for condensed steam taking into account heat losses into the reservoir and overburden formation and hence the fluid production rate changing in time.

Heavy oil or bitumen is recovered by injecting an oil recovery formulation comprising ammonia and steam having a vapor quality of from greater than 0 to less than 0.7, or injecting components thereof, into an underground oil-bearing formation comprising oil or bitumen having a total acid number of at least 0.1 and producing oil or bitumen from the formation after injection of the oil recovery formulation, or components thereof, into the formation.

An evaporator includes plates disposed in pairs in first and second groups, along spaced tanks. Dimples extend from the interior portions in the first group, and interior fins are disposed against the interior portions of the second group. The dimples enhance the distribution of liquid refrigerant in the passageways and the thermal energy exchange between ambient air and an upstream, low vapor quality flow of fluid passing between upstream and downstream side edges, of the first group of plates. The evaporator also eliminates the tonal noise or whistle under certain transient operating conditions.

In delivery of bulk liquefied gas under pressure from portable containers, the claimed invention provides a system and process for directing the evaporated vapor from one or more satellite pressure vessels through a master vessel. The gas transfer operates passively to provide for longer unattended run times for a downstream application. The master vessel serves as a trap for the incoming gas vapor, and thereby improves the overall vapor quality by re-equilibrating the vapor with the colder bulk liquid in the master vessel before delivery to the destination application.

An evaporator using a CO₂ refrigeration that prevents a raise in vapor quality of refrigeration in an evaporator passage to obtain heat exchanging efficiency. The evaporator for use in a refrigeration system includes a refrigerant inlet for introducing a refrigerant, a refrigerant outlet for discharging the refrigerant, and an evaporator passage for causing the refrigerant introduced via the refrigerant inlet to evaporate and leading the refrigerant to the refrigerant outlet. An intermediate outlet is provided at an intermediate portion of the evaporator passage. A refrigerant high in vapor quality among the refrigerant passing through the intermediate portion from the refrigerant inlet flows out of the intermediate outlet to prevent a raise in vapor quality of refrigerant.

An air conditioning system has one expansion valve supplying refrigerant to two evaporators. A vapor quality of a refrigerant has an initial value at a primary inlet of a primary evaporator, and has a resultant value at the primary outlet. The primary evaporator has a bypass inlet at a first location where the vapor quality of the refrigerant is less than about 80% of the resultant value. A secondary evaporator has a secondary inlet receiving a bypass portion of the metered flow of refrigerant split-off at a second location of the primary evaporator between the first location and the expansion valve. The secondary outlet is connected to the bypass inlet. Thus, cooling can be achieved for two different zones using only one expansion valve.

Determination of steam quality by passing one or more laser beams through steam in a steam chamber and directly determining a total number of vapor molecules and a total number of water molecules based on absorption of radiation in the one or more laser beams by the water vapor phase and the liquid water phase in the steam. Specific volumes of water vapor phase and liquid water phase in the steam using the total numbers of water vapor and liquid water molecules are determined and the quality of the steam is calculated based on the specific volumes of the water vapor phase and the liquid water phase in steam. One embodiment comprises a narrow linewidth laser for measuring steam quality and another embodiment comprises multiple broadband lasers for measuring steam quality.

The invention provides a method for a thermally activated closed loop heat transfer system, and requires no other external power source other than the heat which it is transferring. The system is based on a two-phase (liquid/vapor) working fluid, with heat input through an evaporator and heat rejected through a condenser. All of the mechanical power produced by an engine, driven by the high vapor quality fluid leaving the evaporator, is consumed by the pump. The pump drives the low vapor quality fluid leaving the condenser back to the evaporator. Nearly isothermal heat transport can be achieved when using a pure or azeotropic working fluid, since the operation only requires the evaporator pressure to be marginally higher than the condensers pressure.

A heat pipe with a glass shell is composed of a glass shell, a heat-conducting working fluid, and the like. Its glass shell heat pipe is fully sealed by a glass tube head at one end, and then connected to a full glass tube cavity that is exhausted and filled with a heat-conducting working fluid tailpipe after being closed by a glass tube head at the other end. The heat-conducting working medium tailpipe is evacuated, filled with heat-conducting working medium, and then the glass is welded and sealed to form an all-glass circular tubular container. The heat-conducting working medium filled in the heat pipe of the glass shell has the characteristics of large vaporization enthalpy, good thermal conductivity and stable physical and chemical properties. The heat-conducting working medium is either water, an aqueous solution, or a liquid organic substance; the filling amount of the heat-conducting working medium in the heat pipe of the glass shell: the heat-conducting working medium corresponding to the saturated heat-conducting working medium vapor volume of the glass-shell heat pipe under the maximum rated working temperature and pressure steam quality. The heat-conducting working medium steam above the maximum rated working temperature and pressure is superheated steam, and the relationship between its corresponding temperature and pressure follows Charles' law in gas experiments.

A cooling regulation system (100) is described which includes: a valve (110) having an control device (120) configured for controlling an opening of an orifice (111) provided between a valve inlet (112) and a valve outlet (113) such that a flow of a coolant from the valve inlet to the valve outlet can be regulated; an evaporator (130) with a contact surface that is adapted to be thermally connected to a heat source (140, 141) such that a thermal load from the heat source is dissipated by the evaporator in an operating state of the cooling regulation system; and a regulation device (150) configured for regulating a position of the control device in order to regulate the flow of the coolant, wherein the regulation device is in thermal contact with the evaporator at a position at which a vapor quality [chi] of the coolant is [chi]<=[chi]cr, wherein [chi]cr is the critical vapor quality.

A method of determining a steam quality of a wet steam located in an interior of a steam turbine includes emitting from an optical probe a plurality of wavelengths through the wet steam, measuring with the optical probe a wet steam intensity corresponding to each of the plurality of wavelengths emitted through the wet steam, determining an intensity ratio vector by dividing the wet steam intensity by a corresponding dry steam intensity for each of the plurality of wavelengths, successively applying scaling factors to the intensity ratio vector to obtain a scaled intensity ratio vector, calculating a suitable value for each of the scaling factors to obtain a plurality of residuals, determining a minimum residual of the plurality of residuals, determining a droplet size distribution by calculating the droplet number density corresponding to the minimum residual, and determining the steam quality based on the droplet size distribution.

The invention provides an on-line testing method for a sodium analyzer. 65-75wt% diisopropylamine and 45-55wt% diisopropylamine are respectively used as the alkali agents for air-ventilating and alkali-adding on-line testing for the sodium analyzer and air-evacuating and alkali-adding on-line testing for the sodium analyzer. The method is capable of not only meeting the requirement of the sodium ions testing for water alkalinity but also reducing the instrument testing error so as to improve the instrument testing reliability. In addition, the correct values of sodium ions testing can help an operator to discover the problems of aqueous vapor quality control and adjust the work mode promptly, thereby reducing the corrosion, scale formation and salification of each machine set each year, so as to avoid an economic loss of millions of Yuan, have a significant importance in the safe and economical operation of a power plant as well as save energy and reduce consumption.

The invention provides a thermal power plant vapor quality monitoring method and system. Through introduction of gray system indexes and combination of a weight adjustment algorithm, a gray system including the weight adjustment algorithm no longer depends on single index measuring points and expert database data for inferring equipment faults, however, other multi-index measuring points are added to serve as characteristic parameters for unified inferential analysis, a gray relational coefficient of set weight values and a parameter sequence is calculated, then an expert system infers and defines calculated relational coefficient weight adjustment value, and a monitoring analysis conclusion is obtained finally to enable fault information covered by vapor quality change to be deeper, so that a thermal power plant vapor quality monitoring conclusion is more accurate.

The invention relates to the field of steam injection thermal recovery of thickened oil, in particular to a method and device for determining the temperatures of the upper end and the lower end of a gas injection well packer. The method includes the steps that the temperature field distribution of steam in a gas injection well heat insulation pipe is acquired; the temperature field distribution of the outer wall of the heat insulation pipe and the temperature field distribution of the inner wall of a casing pipe are acquired according to the temperature field distribution of the steam in the heat insulation pipe; the temperature of the lower end of the packer and the temperature of the upper end of the packer are acquired according to the temperature field distribution of the outer wall of the heat insulation pipe and the temperature field distribution of the inner wall of the casing pipe. According to the method, the temperature of the upper end of the packer and the temperature of the lower end of the packer are calculated, and therefore the position of the packer can be optimized; the method is of great guiding significance on improvement of the heat insulation effect of a gas injection well, prolonging of the thermal recovery life of an oil well and improvement of the quality of steam and the oil well thermal recovery effect.

A condensation system for a reservoir, which stores fuel cryogenically, is disclosed. A portion of the fuel exists as a boil-off gas with a first vapor quality. The condensation system includes an absorption unit coupled to the reservoir and is configured to receive and mix the boil-off gas with a refrigerant, forming a liquid solution. A distillation unit is coupled to the absorption unit to receive the liquid solution at a supplemented pressure, and is configured to separate the fuel to a gaseous state from the liquid solution. Further, a cooling circuit is configured to receive the fuel in the gaseous state from the distillation unit at the supplemented pressure and a supplemented temperature, and deliver the fuel to the reservoir at a lower pressure and a temperature, with a vapor quality lower than the first vapor quality.

The present invention utilizes mechanical vapor compression and/or thermal vapor compression integrating compression loops across multiple process stages. A sequential network of compressors is utilized to increase the pressure and condensing temperature of the vapors within each process stage, as intra-vapor flow, and branching between process stages, as inter-vapor flow. Because the vapors available are shared among and between compressor stages, the number of compressors can be reduced, improving economics. Balancing vapor mass flow through incremental compressor stages which traverse multiple process stages by splitting vapors between compressor stages enables the overall vapor-compression system to be tailored to individual process energy requirements and to accommodate dynamic fluctuations in process conditions.