7results about "Hydrocarbon dewatering" patented technology

A system for refining crude oil to minimize emissions of toxic compounds in the atmosphere during refining. The crude oil is treated with viscosity-reductant additives, reducing viscosity by up to 50% and increasing API gravity by more than 2 points. The method of spray-cracking and vacuum-flashing of crude oil, the system separates light and heavy end chains within the reactor. The vapor is condensed into designer fuels using a multi-stage horizontal reverse condensate-condenser or closed-loop distillation tower. Process heater directs flue gases through high-salinity fluids, such as a brine-processing device to capture, sequester, or mineralize the CO2, CO, NOx, and other contaminants from the flue gases. This results in a significant reduction in emissions, a further reduction to near-zero emissions (>95-98%) is achieved by the combination of (1) the closed loop processes, tank blanketing and capturing, sequestering and mineralizing emitted flue gases from the heater combustion-exhaust.

The application discloses a light hydrocarbon gas production system, which comprises a liquid storage tank, a gas storage tank, an air compressor, a drying cavity, a heat exchanger and a gas-liquid separation tank. Liquid fuel is heated and gasified by hot air in the heat exchanger, and is mixed with cooled air to form gasified fuel. The energy in the hot air generated by the air compressor of the production equipment in the workshop is fully utilized, and the cost is effectively reduced.

The application discloses a tar distillation process for improving oil quality, and relates to the technical field of deep processing of coal tar. The process is a coal tar atmospheric and vacuum distillation process for full distillation of unwashed three-mixed oil on the top of a tar distillation column. The core of the process is that, without changing the main structure of the original distillation equipment, four core process parameters, including backflow, vacuum degree at the top of the column, temperature at the bottom of the column and temperature at the top of the column, are simultaneously and cooperatively controlled in the vacuum distillation process of the tar distillation column, and the distillation quality control thresholds of unwashed three-mixed oil and carbon black oil are matched and set. The application solves the problems of wide process parameter control, low and unstable product quality of the existing tar distillation process, and can make the downstream washed oil product reach the first-grade product requirement in the GB / T24217-2025 standard, while not affecting the raw material adaptability of carbon black oil to the downstream modified pitch device. The application has the advantages of low modification cost, easy industrialization, stable product quality and remarkable economic benefits.

A positive pressure heating crude oil stabilization system parameter optimization method and device, the method comprises the following steps: constructing a crude oil stabilization simulation model of a positive pressure heating crude oil stabilization system, at least including a stabilization tower module and a pre-tower heating furnace module; inputting crude oil component parameters into the crude oil stabilization simulation model, and setting the heating furnace outlet temperature as different temperature values T n sequentially; n Carrying out positive pressure heating crude oil stabilization process simulation to obtain the stabilization tower overhead pressure P n and fuel consumption F n corresponding to the highest light hydrocarbon yield Q n at each temperature value T n ; calculating the corresponding profit value A n according to each set of yield and energy consumption data, each set of yield and energy consumption data comprising Q n and F n ; obtaining the maximum profit value from N profit values A n , and taking the T n and P n corresponding to the maximum profit value as the optimal heating furnace outlet temperature and the optimal stabilization tower overhead pressure respectively; and based on the crude oil stabilization simulation model, analyzing the light hydrocarbon yield and fuel energy consumption to ensure the maximum economic benefit while saving energy and reducing costs.

The application discloses a light hydrocarbon gas production equipment, which comprises a liquid storage tank, a gas storage tank, an air compressor, a drying cavity, a heat exchanger, a cooling tower and a gas-liquid separation tank. The heat of the air compressor is utilized to heat the water circulating in the heating water pipe. The heated water exchanges heat with the liquefied fuel in the heat exchanger, so that the liquefied fuel is gasified and mixed with the injected dry high-pressure gas to form gasified fuel. The energy in the hot air generated by the air compressor of the production equipment in the workshop is fully utilized, and the cost is effectively reduced.