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79 results about "Water equivalent" patented technology

Water equivalent. noun. : the product of the mass of a body by its specific heat equal numerically to the mass of water that is equivalent in thermal capacity to the body in question.

Irrigation water management system based on farmland water monitoring, and management method implemented by system

The invention discloses an irrigation water management system based on farmland water monitoring, and a management method implemented by the system. The system comprises a soil water and soil temperature information module, a farmland irrigation and soil water content information module, an irrigation area water consumption and irrigation result measuring and reporting module, and an irrigation area irrigation benefit result reporting module. The system and the method provided by the invention have the advantages that through comprehensive and modular technical methods and solutions, the maximum application of limited information is achieved; an information source, data transmission, a server and a database are utilized to provide basic conditions for storage, extraction, utilization and processing of monitoring information demand responses by the management system; and through comprehensive technical analysis methods, such as water balance, logical association, mathematical statistics, the method of measuring soil water contents at the beginning and the end of a period, the head-tail ratio calculation method, cross-industry data application, the water equivalent calculation method and the like, analysis of a water consumption quota, an irrigation system, the soil water content, the amount of water required by crops, an irrigation water utilization coefficient, the amount of water introduced into an irrigation area, crop yields, irrigation benefits and other management technology evaluation indicators can be achieved.
Owner:XINJIANG INST OF WATER RESOURCES & HYDRAULIC POWER

Food grade lubricating grease and its preparation method and application

ActiveCN102268320AComply with water quality sanitation and safety requirementsSealedLubricant compositionFood gradeBase oil
The invention relates to food-grade lubricating grease as well as a preparation method and application thereof. The food-grade lubricating grease comprises the following components by weight percent: 70-80% of base oil, 6-15% of thickening agent and 10-20% of antiwear agent. The preparation method comprises the following steps: adding fatty acid, aromatic acid and organic aluminum into the base oil in a proportion, mixing and heating to 60-100 DEG C, and carrying out a recombination reaction for 1-2 hours; further heating the combined material to 100-140 DEG C, adding tap water with a certain proportion and then maintaining the constant temperature for 1-2 hours, wherein water equivalent is 1-3 times that of organic aluminum; further heating the combined material to 150-180 DEG C and the nmaintaining the constant temperature for 0.5-1 hour; then adding quenching oil and evenly mixing, wherein the amount of quenching oil is about 30%-40% of that of base oil; and further cooling the material to the temperature below 140 DGE C, and adding the antiwear agent and then evenly mixing, so as to obtain the required product. In the invention, a one-step method is adopted for direct recombination reaction, thus process is simple, energy consumption is reduced, production cost is reduced, and the quality of the product produced by the process is relatively stable.
Owner:CHINA PETROLEUM & CHEM CORP

Ion beam radiotherapy dosage verification method based on water equivalent coefficients

The invention relates to an ion beam radiotherapy dosage verification method based on water equivalent coefficients. The ion beam radiotherapy dosage verification method based on the water equivalent coefficients includes the following steps that A, CT image data of a cancer patient are obtained, a treatment planning system (TPS) is utilized for plan design according to a CT-water equivalent coefficient transformation curve, and ion beam radiation parameters are recorded after the plan is determined; B, a virtual three-dimensional water phantom CT image is generated based on the water equivalent coefficients, the ion beam radiation parameters are transplanted to the water phantom through the TPS, dosage optimal computation is carried out again, and three-dimensional rasterization dose distribution in the water phantom is obtained; C, an ionization chamber is placed at an interest point in the three-dimensional water phantom, interpolating calculation is carried out in the three-dimensional rasterization dose distribution according to the three-dimensional coordinates of the sensitive volume of the ionization chamber in the water phantom, and planned dosage of the interest point is obtained; D, the ion beam radiation parameters designed as planned control a medical heavy-ion accelerator to perform simulated irradiation on the water phantom, and the measured absolute dosage value of the interest point for the ionization chamber in the water phantom is compared with the planned dosage.
Owner:INST OF MODERN PHYSICS CHINESE ACADEMY OF SCI

System and method for constant water level sequential batch type sewage treatment system with continuous variable volume

The invention discloses a system and a method for constant water level sequential batch type sewage treatment system with continuous variable volume. The method includes continuously injecting sewage into a constant water level variable volume adjusting area to enable an adjustable volume area to float on the liquid level in separation mode, injecting water to a constant water level variable volume reaction area through a distribution pump, injecting water to a constant water level variable volume water quality stabilizing area through a constant water level water decanting device and a waterdecanting pump, enabling supernate after reaction to be discharged into the supernate of the a constant water level variable volume water quality stabilizing area on the other side of the constant water level variable volume reaction area, pass through a smoothing clearing area and finally pass through an inclined plate clearing area and continuously discharging purification water equivalent withpreprocessing feeding water. The system and the method resolve the technical problem that denitrification and dephosphorization efficiency is low, single process structure water outlet index cannot meet requirements of indexes of the national standard first grade A, and process structure is complex. The system has the advantages of being simple in structure, low in integral process energy consumption, good in processing effect and the like.
Owner:鲍洪泉

Rectifying type variation-concentration self-overlaying gas liquefaction system

The invention discloses a rectifying type variation-concentration self-overlaying gas liquefaction system which comprises a compressor, a condenser, a rectifying device and a feed gas liquefaction loop, wherein the feed gas liquefaction loop comprises a first heat exchanger group, a second heat exchanger group and a first throttle valve arranged between the first heat exchanger group and the second heat exchanger group; and two parallel arranged first variable concentration loop and second variable concentration loop are arranged between the rectifying device and an air suction hole of the compressor. The rectifying device is used for replacing a multistage separation process of the traditional mixed refrigerant gas liquefaction system, and different components of high-pressure liquids are led from the bottom and the top of the rectifying device and are respectively subjected to pressure reduction and then enter the two heat exchanger groups, water equivalent change of a feed gas cooling and liquefaction process is optimized and matched, and variable working condition regulating capacity of the liquefaction system is improved by adopting the variable concentration loops. The invention has the advantages of simple structure, operation reliability, high system liquefaction efficiency and the like, and is suitable for various small and minitype gas liquefaction systems with high performance requirements on variable working conditions.
Owner:ZHEJIANG UNIV

Rectification-type self-overlaying gas liquefying system

The invention discloses a rectification-type self-overlaying gas liquefying system, which comprises a compressor, a condenser, a rectifying device and a raw material gas liquefying loop. A discharging port of the compressor is connected with a feeding port of the condenser; a discharging port of the condenser is connected with a feeding port in a kettle of the rectifying device; the rectifying device comprises a rectifying tower and a tower top heat exchanger, wherein the tower top heat exchanger is communicated with the top of a rectifying section of the rectifying tower; a discharging port at the top of the tower top heat exchanger is connected with the raw material gas liquefying loop; and the raw material gas passes through the raw material gas liquefying loop and a final liquefying product is obtained. In the invention, a multi-stage separation process of the traditional mixed working medium liquefying system is replaced by the rectifying device, the high-pressure liquids with different components led out from the bottom and the top of the rectifying device are respectively subject to pressure reduction to enter the raw material gas liquefying loop, the change of the water equivalent weight in the temperature-reduction liquefying process is matched in an optimized way so that the raw material gas is cooled section by section. The rectification-type self-overlaying gas liquefying system has the advantages of simple structure, reliability in operation, high system liquefying efficiency and the like, and is particularly suitable for various mini-type and micro-type gas liquefying systems.
Owner:ZHEJIANG UNIV

Preparation method of zero-VOC high-performance alcoholic acid emulsion

The invention discloses a preparation method of a zero-VOC high-performance alcoholic acid emulsion. The preparation method comprises the following steps: firstly, performing alcoholysis on a drying oil or a semi-drying oil and a polyhydric alcohol under the action of a high temperature and an alcoholysis catalyst, and then performing an esterification reaction with polybasic acid to obtain an air-drying alkyd resin; next, moving the alkyd resin to a reaction kettle with a circulating water jacket, heating the circulating water in the jacket of the reaction kettle until an emulsification temperature, controlling the rotating speed to the range of 170rpm to 180rpm, adding a neutralizer to the reaction kettle and mixing thoroughly and evenly; keeping the temperature unchanged, and adding a proper amount of emulsifier to the reaction kettle, adjusting the rotating speed to the range of 250rpm to 270rpm, and stirring for 30 to 45 minutes; heating deionized water equivalent to the resin by mass until an emulsification temperature and slowly and dropwise adding the deionized water to the reaction kettle at a constant speed in about 3-5 hours; and furthermore, cooling in water bath under stirring until a room temperature, regulating the pH value of the emulsion by use of a pH regulator to the range of 5-7, and filtering to obtain the zero-VOC high-performance alcoholic acid emulsion. According to the preparation method, zero VOC emission is really realized in the production and application processes.
Owner:青岛乐化科技有限公司 +3

Variable water temperature control system suitable for air conditioning secondary pump system

The invention provides a variable water temperature control system suitable for an air conditioning secondary pump system, relates to the field of refrigeration control, and aims to improve the refrigerator power and hydraulic equilibrium adjusting accuracy of an air conditioning system and reduce energy consumption. The variable water temperature control system comprises a refrigerator device, a water supply/return pipeline, the air conditioning system and an equalizing pipeline. The air conditioning system comprises one or more air conditioning terminals, and the air conditioning terminals are of multiple types including fan coil pipes. A primary water pump and a secondary water pump are arranged on the water supply/return pipeline. The control system further comprises a refrigerator power preprocessing device, a refrigerator power control device and a secondary water pump variable-frequency control device, the refrigerator power preprocessing device is used for calculating the reflux ratio of the equalizing pipeline and the cold water temperature set value, and the refrigerator power control device is used for controlling the power of the refrigerator device. The secondary water pump variable-frequency control device is used for calculating the cold water equivalent valve position opening degree value of the fan coil pipes, and variable-frequency control is carried out over the secondary water pump according to the maximum valve position opening degree value in all air conditioning terminal cold water adjusting valves in the air conditioning system. The variable water temperature control system can be used for a frequency conversion technology in air conditioning.
Owner:XINZHI ENERGY SYST CONTROL

Method for improving regional groundwater reserve estimation precision

The invention discloses a method for improving regional groundwater reserve estimation precision. The method comprises the following steps of: acquiring monthly-scale land water reserve change delta TWS0; extracting monthly-scale soil water content change delta SM1, snow water equivalent change delta SWE1 and vegetation canopy water reserve change delta PCSW1 in a global range by utilizing a GLDAShydrological model; extracting monthly-scale soil water content change delta SM2, snow water equivalent change delta SWE2 and vegetation canopy water reserve change delta PCSW2 in a global range by utilizing a WGHM hydrological model; calculating to obtain monthly-scale underground water reserve changes delta GWS1 and delta GWS2; evaluating the delta GWS1 and the delta GWS2 respectively accordingto the actually measured monthly-scale groundwater reserve change delta GWS0 in a research region; and selecting the optimal monthly-scale groundwater reserve change delta GWS as a monthly-scale groundwater reserve change result of each pixel of the research region according to the evaluation result, and outputting the monthly-scale groundwater reserve change result. According to the method, theestimation precision of the regional groundwater reserves is improved based on the statistical selection method in combination with GRACE satellite gravity data and a global hydrological model.
Owner:CHINA ACADEMY OF SPACE TECHNOLOGY

Rectification type auto-cascade low-temperature condensation oil-gas separation system with cooling capacity recovery

The invention discloses a rectification type auto-cascade low-temperature condensation oil-gas separation system with cooling capacity recovery. The system comprises a compressor, a condenser, a rectification device and an oil-gas condensation separation and cooling capacity recovery loop, wherein the oil-gas condensation separation and cooling capacity recovery loop comprises a first heat exchanger unit, a second heat exchanger unit, a third heat exchanger unit, a first restricting element and a separator unit. According to the system, the rectification device is adopted to replace multi-stage separation process of a conventional mixed working medium auto-cascade oil-gas separation system, meanwhile high-pressure liquid refrigerants of different components are respectively led out from the bottom and the top of the rectification device, condensed oil is precooled, is respectively depressurized, is fed into the first heat exchanger unit and is optimized to be matched with water equivalent weight variations of oil gases of different components in the cooling process. The system has the advantages of being simple in structure, reliable in operation, good in energy conservation and the like, and is particularly applicable to treatment on volatile oil gases in places such as oil depots, petrol stations and chemical treatment plants.
Owner:ZHEJIANG UNIV +1

Inversion method of original permeability of gas-water two-phase seepage stress sensitive reservoir

The invention relates to an inversion method of the original permeability of a gas-water two-phase seepage stress sensitive reservoir. The method comprises the steps that (1), daily production data ofa gas well, reservoir physical properties, fluid properties, and stress sensitive data are collected and collated; (2), gas-water equivalent permeability curves under different pressure conditions are calculated; (3), improved pseudo parameters taking gas-water two-phase complex seepage characteristics of the stress sensitive reservoir into consideration are calculated; (4), drawing is conductedand an improved semi-logarithmic curve is utilized to identify pseudo radial flow; (5), linear regression is performed on scatters on the curve, and a reservoir original permeability calculation modelis utilized to achieve the inversion of the original permeability according to the slope of a straight line obtained by the regression. According to the method, the complex seepage characteristics such as stress sensitivity of a relative permeability curve, absolute permeability stress sensitivity, a slippage effect and the like can be fully considered, errors caused by a traditional calculationmethod are eliminated, and the method can be extensively applied to reservoir parameter evaluation of the stress sensitivity reservoir.
Owner:CHANGZHOU UNIV

Inversion method for fracture half-length of water production fracturing gas well in stress sensitivity storage layer

The invention relates to an inversion method for the fracture half-length of a water production fracturing gas well in a stress sensitivity storage layer. The method comprises the following steps that(1) daily production data of the gas well, physical properties of the storage layer, physical properties of fluid and stress sensitivity data are collected and sorted out; (2) gas-water equivalent relative permeabilities under different pressure conditions are calculated; (3) improved simulation parameters considering gas-water two-phase complex seepage characteristics of the stress sensitivity storage layer are calculated; (4) an improved radical sign time curve is drawn and used for identifying a stratum linear flow; (5) data points at the stratum linear flow stage are subjected to linear regression, based on an obtained straight slope, calculation is conducted by using an inversion model, and inversion of the fracture half-length is achieved. According to the inversion method, complexseepage characteristics such as relative permeability curve stress sensitivity, absolute permeability stress sensitivity and slippage effect during gas-water two-phase seepage in the stress sensitivity storage layer can be comprehensively considered, errors caused by a traditional calculation method are removed, and the method can be widely applied to post-pressing evaluation of the water production fracturing gas well of the stress sensitivity storage layer.
Owner:CHANGZHOU UNIV
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