352 results about "Heat torch" patented technology

Systems and methods of the present disclosure includes a mixer configured to mix air and hydrocarbons and a burner configured to receive the mixed air and hydrocarbons and to generate syngas. The system also includes a cooling system configured to receive the syngas and to cool the syngas to form cooled syngas. The system further includes a collector configured to collect carbon from the cooled syngas as soot. Moreover, the system includes a flare stack configured to receive the cooled syngas and to burn off at least part of the cooled syngas.

The invention discloses a remote ignition control system for a release flare, and relates to the technical field of release flare control, the system comprises the following components: a fault detection module, a fault isolation module, a standby module, a redundant circuit switching module, a fault diagnosis module and a wireless communication module; by integrating multiple modules of fault detection, fault isolation, standby module and redundant circuit switching, fault diagnosis and wireless communication, comprehensive remote monitoring and management of the release flare ignition control system are achieved, when the system detects a fault, electrical connection of a fault component can be rapidly cut off, and the safety of the release flare ignition control system is improved. And the standby module or the redundant circuit is automatically switched, so that the continuous and stable operation of the system is ensured, the reliability and the safety of the system are remarkably improved, and the risk of production interruption caused by faults is reduced.

This flame-retardant resin composition comprises a thermosetting resin and a flame-retarding agent, and has a ΔEr value of 30 or less as determined by the following procedure. Procedure: (i) A test plate (size: 120 mm square, 2 mm in thickness) under the conditions including a mold temperature of 175°C and a curing time of 3 minutes is prepared using the flame-retardant resin composition. (ii) A torch burner (30 mm with respect to a flame length of about 100 mm) is set to the center of one surface of the vertically-set test plate such that the angle with respect to the test plate becomes 90°, and a flame from the torch burner is applied to the center for 5 minutes. (iii) For the center of the other surface of the test plate and two points which are located on a straight line passing through the center of the other surface of the test plate and are each 3 mm away from this center, color differences between before and after the contact with the flame are separately measured and an average value (ΔEr) is determined.

The utility model discloses a black water waste heat high-quality recycling system which comprises a high-pressure purification flash evaporator, a low-pressure purification flash evaporator, a high-flash tank and a low-flash tank, black water is sequentially subjected to four times of flash evaporation stripping, flash steam generated by the high-pressure purification flash evaporator and flash steam generated by the low-pressure purification flash evaporator respectively act with an evaporator to generate saturated steam, and the saturated steam is separated from the low-flash tank. The saturated steam can meet different process applications after being pressurized by the steam pressurizing device; the high-flash condenser is used for condensing high-flash steam discharged by the high-flash tank, non-condensable gas enters a torch treatment pipeline, and condensed water is recycled in the process; the low flash tank is used for receiving the liquid part discharged by the high flash tank; the low-flash condenser is used for condensing low-flash steam in the low-flash tank and then returning the condensed low-flash steam to a process system for recycling; and the demineralized water preheater is used for receiving part of the low-flash liquid discharged by the low-flash tank to preheat the demineralized water. According to the utility model, the waste heat of black water can be extracted in a grading manner and efficiently utilized.

Systems and methods of the present disclosure includes a mixer configured to mix air and hydrocarbons and a burner configured to receive the mixed air and hydrocarbons and to generate syngas. The system also includes a cooling system configured to receive the syngas and to cool the syngas to form cooled syngas. The system further includes a collector configured to collect carbon from the cooled syngas as soot. Moreover, the system includes a flare stack configured to receive the cooled syngas and to burn off at least part of the cooled syngas.

The invention discloses a rotary kiln pyrolysis process preheating and replacing method which comprises the following steps: replacing and preheating an upgrading system when a rotary kiln is started, performing low-load operation on the rotary kiln, heating the rotary kiln by a rotary kiln hot blast stove and a flue gas fan, closing a pipeline valve from a dry gas fan to a first dust remover, and performing low-load operation on the rotary kiln; a rotary kiln nitrogen replacement valve is slightly opened, nitrogen enters the rotary kiln through a dry gas guide screw for replacement and heat removal, an oil and gas pipeline is preheated, direct cooling tower spraying cooling water and indirect cooling tower circulating cooling water are put into use, a coal gas fan is started for system circulation, and an electrical tar precipitator outlet is opened to a rotary kiln starting line valve; the invention further discloses a rotary kiln quality improvement system, the rotary kiln pyrolysis process preheating and replacement method is adopted, the start-up time is effectively shortened, the investment and operation cost is saved, and meanwhile a foundation is laid for long-period stable operation of the system.

Techniques of processing a flare gas include operating a flare gas piping network to output a flare from a plurality of flows of a purge gas in purge gas headers coupled to a main header, and during operation of the flare gas network to output the flare from the plurality of flows of the purge gas: obtaining a fluid pressure of the flow of the purge gas at each purge gas header; obtaining a fluid temperature of the flow of the purge gas at each purge gas header; and obtaining a rate of the flow of the purge gas at each purge gas header; and based on the obtained fluid pressures, fluid temperatures, and rates of the flows of the purge gas, determining an optimized flow velocity of the purge gas at each of the plurality of purge gas headers.

The invention discloses an integrated anaerobic fermentation self-heating biogas production system and method, and belongs to the technical field of biomass energy. In the system disclosed by the invention, a thermal medium outlet of a solar heat collection unit is connected with a thermal medium inlet of a heat storage unit; a heat medium outlet of the heat storage unit is connected with a heat medium inlet of the anaerobic fermentation unit; a gas outlet of the anaerobic fermentation unit is respectively connected with the post-treatment system and the torch incineration device; a natural gas outlet of the post-treatment system is connected with the torch incineration device; a waste heat outlet of the post-treatment system is connected with a thermal medium inlet of the anaerobic fermentation unit; a cold medium outlet of the anaerobic fermentation unit is connected with a cold medium inlet of the heat storage unit; and a cold medium outlet of the heat storage unit is connected with a cold medium inlet of the solar heat collection unit. The system solves the technical problem that an existing method is high in energy consumption and difficult to achieve efficient operation of the whole system.

The invention designs an environment-friendly blowout device suitable for a high-salinity gas well, and belongs to the technical field of unconventional petroleum and natural gas extraction. The device comprises a two-stage concentric liquid remover and a combustion purification system which are connected in sequence. The two-stage concentric liquid remover realizes efficient separation of gas, liquid and solid phases through two-stage centrifugal separation. And a self-adaptive liquid discharge and gas control mechanism is arranged at the bottom of the two-stage concentric liquid remover, so that flow fluctuation self-adaptive sealing can be realized. Pretreated gas enters a combustion tank, is discharged through a torch pipe and is ignited, and generated combustion gas and solid particles are sprayed and purified in all directions and sprayed liquid is recycled through a spraying and recycling device above the combustion gas and the solid particles. The device integrates multiple technical functions such as buffering and pressure stabilizing, multi-phase separation, all-directional spraying purification, fire-liquid isolation, flow fluctuation self-adaption, automatic sealing, explosion prevention and fire retardance, the three-phase separation efficiency is remarkably improved, salting-out particles entering the environment are reduced, and equipment and technical supports are provided for green development of a hypersalinity gas well.

The invention discloses a low-temperature flare gas heat exchange device based on a U-shaped heat exchange tube and a method thereof, and belongs to the technical field of cryogenic equipment. The heat exchange device provided by the invention comprises a barrel body, a sealing head, a tube pass tube box, a tube pass tube plate, a heat exchange tube, a steam tube and a steam injection tube, wherein the heat exchange tube is a U-shaped heat exchange tube. The upper part of the cylinder is provided with a steam pipe through hole and a pressure balancing vent hole, and the bottom of the cylinder is provided with a water injection port and a drain outlet. And a heat exchange tube is arranged in an inner cavity of the cylinder body and is communicated with the tube pass tube box through a tube pass tube plate. The lower end and the upper end of the tube pass tube box are respectively connected with the air inlet pipe and the air outlet pipe; the ends, away from the tube pass tube plate, of the heat exchange tubes are provided with anti-short-circuit partition plates. A liquid level control interface is arranged on the side surface of the barrel. The heat exchange device provided by the invention is compact in design, space is saved, the use of materials is reduced, the manufacturing process is simplified, the heat transfer efficiency is improved, the performance is improved, the heat exchange device has remarkable economical efficiency and high performance advantages, and the manufacturing cost is reduced.

The invention relates to a pure oxygen pulverized coal burner which comprises a pulverized coal bin, a pulverized coal conveying cylinder, an oxygen header pipe, oxygen spray pipes and burner blocks. The oxygen spray pipe and the pulverized coal conveying cylinder extend into the burner block; a pulse valve is arranged on the oxygen spraying pipe, an accumulation groove and a pulverized coal striking head are arranged at the tail end of the pulverized coal conveying barrel, pulverized coal falls into the accumulation groove through conveying of the pulverized coal conveying barrel, and the pulverized coal striking head is connected with a striking head driving motor through a striking head transmission shaft to rotate at a high speed to strike the pulverized coal falling into the accumulation groove. Compared with the prior art, the pulse jet oxygen is supplied after the pulverized coal is scattered and scattered, so that the torch time is effectively shortened, and the thermal radiation of a continuous combustion torch to a nozzle is eliminated to a great extent. The supply of the pulverized coal and the supply of the oxygen can be flexibly controlled through the opening and closing interval time of the valve, and the power of the combustor can be conveniently adjusted according to the required furnace temperature and heat supply amount, so that the oxygen and the pulverized coal can be fully and uniformly mixed regardless of the power, and the optimal air-fuel ratio is achieved.

The present invention discloses a device and method for recovering the coldness of residual liquid in a synthesis gas CO cryogenic separation system, and belongs to the field of chemical process. When the synthesis gas CO cryogenic separation system is shut down and drained, the temperature can reach -190°C due to the large amount of low-temperature residual liquid stored in the cold box. The conventional treatment method is to send the low-temperature residual liquid to the flare gas heater through ambient gasification, and discharge it as room-temperature flare gas after heat exchange with saturated steam. When the amount of low-temperature residual liquid is large, this method takes a long time to vaporize the low-temperature residual liquid; or nitrogen is used to cool and gasify the low-temperature residual liquid to produce low-temperature flare gas, which is then sent to the flare gas heater for heat exchange. This method increases nitrogen loss, increases the load of the flare gas heater, makes its equipment size larger, and increases cost. The present invention utilizes the high-grade low-temperature coldness of the low-temperature residual liquid in the CO cryogenic separation system to convert room-temperature nitrogen into liquid nitrogen for storage and recovery, thereby reducing nitrogen loss, reducing 0.5MPaG steam loss, and reducing flare gas emissions.

1. The name of the design product: biogas torch (premixed type). 2. The use of the design product: for processing biogas generated in the production process of sewage treatment plants, waste treatment plants, farms, chemical plants, etc.; biogas generated by anaerobic fermentation in the sewage treatment of pharmaceutical factories, distilleries, paper mills, kitchen waste treatment, landfill leachate, food factories, beverage factories, etc. 3. The design points of the design product: in shape. 4. The picture or photo that best indicates the design points: perspective view 1. 5. The top surface of the design product is not easily visible or invisible during use, and the bottom view is omitted. The bottom surface of the design product is not easily visible or invisible during use, and the top view is omitted.

1. The name of the design product: floor fan (torch style). 2. The use of the design product: for blowing and cooling, etc. 3. The design points of the design product: in shape. 4. The picture or photo that best indicates the design points: perspective view 1.

The present application provides an apparatus and method for recovering nitrogen discharged from waste water by washing with liquid nitrogen, comprising: a U-tube circulating water heater, a first pipeline, and a second pipeline. The inlet end of the U-tube circulating water heater is connected to the middle section of the second pipeline through the first pipeline, and the outlet end is used to connect to the fuel gas pipeline network; one end of the second pipeline is connected to the hydrogen separator; a control valve and a shut-off valve are provided on the second pipeline, and the control valve is located between the first pipeline and the hydrogen separator, and the shut-off valve is located between the first pipeline and the end of the second pipeline away from the hydrogen separator. The present invention effectively recovers CO in the discharged nitrogen. Each set of equipment can recover more than 170 NM3 / h of fuel gas and 100 NM3 / h of effective gas, with an annual benefit of more than 640,000 yuan, and a significant energy-saving effect. At the same time, due to the reduction of cold torch discharge, steam consumption is indirectly saved, and the phenomenon of long-term ice accumulation in the buffer tank is completely eliminated, which greatly improves the sanitation around the buffer tank and on the ground.

The utility model belongs to the technical field of gas detection, and discloses a gas closed sampling device which comprises a medium side valve (1), a flow limiting orifice plate (2), a sampling needle valve (3), a gas-liquid shared quick connector (4), a sampling ball bladder (5), a one-way valve (6) and a torch system valve (7), a medium side valve (1) is arranged at a sampled medium pipeline, a torch system valve (7) is arranged at a torch system, the medium side valve (1) and the torch system valve (7) are connected through a pipeline, a flow limiting orifice plate (2) and a one-way valve (6) are sequentially arranged on the pipeline, and a sampling needle valve (3) is arranged on the pipeline between the flow limiting orifice plate (2) and the one-way valve (6). And the sampling ball bladder (5) is connected with the sampling needle valve (3) through the gas-liquid shared quick connector (4). The device is simple in structure, easy-to-wear parts are reduced, maintenance is convenient, and cost is reduced; the pipeline is thicker than a closed sampler in diameter, so that the pipeline blockage risk is reduced.

This application provides an LNG closed - type ground flare emission device. By setting multiple gas tanks and a gas tank drive mechanism, emission gases of different properties can be introduced into different gas tanks for storage and then burned sequentially, avoiding safety accidents caused by the reaction of different emission gases mixing or the situation of incomplete combustion.

A torch assembly is configured to produce a flame and includes an ignitor assembly having a fuel canister coupling for connection to a fuel canister to produce a flame. A body covers the igniter assembly and extends along a centerline from a first end to a second end opposite the first end. The first end of the body extends longitudinally beyond the fuel canister coupling and encircles the centerline to define an opening for receiving the fuel canister. A burn tube extends from the second end of the body and is in fluid connection with the ignitor assembly for directing the flame out of the burn tube.

The invention discloses a combustion stability evaluation test device and method based on a controllable ignition pressure peak, and the device comprises a combustion unit which is of a hollow cylinder structure with two open ends, and an inner cavity of the combustion unit is a combustion chamber; one port of the combustion unit is coaxially connected with an injector, the side wall of one port of the combustion unit is provided with a torch igniter communicated with an inner cavity of the combustion unit, and the side wall of the non-end portion of the combustion unit is provided with at least one combustion chamber steady-state pressure measuring interface and at least one combustion chamber pulsating pressure measuring interface which are communicated with the inner cavity of the combustion unit. The injector and the torch igniter are matched to adjust the medium filling time sequence of the combustion chamber and the working state of the torch igniter, and the steady-state pressure and the pulsating pressure in the combustion chamber are measured in real time through the combustion chamber steady-state pressure measuring interface and the combustion chamber pulsating pressure measuring interface, so that the control on the peak amplitude of the ignition pressure is realized; ignition impact peaks are integrally and autonomously generated, the function of controlling parameters such as the amplitudes of the ignition pressure peaks is achieved, and the combustion stability under the disturbance conditions of the ignition pressure peaks with different amplitudes is evaluated.

The embodiment of the present application provides a controllable micro-pulse incineration catalytic treatment and waste heat recovery device for the exhaust gas of a transport ship, which relates to the technical field of ship exhaust gas treatment. The controllable micro-pulse incineration catalytic treatment and waste heat recovery device for the exhaust gas of a transport ship includes a pulse incinerator boiler, an ignition power supply device, and a heat exchange tube; the pulse incinerator boiler serves as the core load-bearing structure for integrating the ignition power supply device and the chimney; the ignition power supply device is integrally installed in the pulse incinerator boiler. This solution realizes efficient incineration, deep oxidation purification of the catalyst layer, and cascade recovery of waste heat in the heat exchange tube by dynamically adjusting the gas mixing ratio, solves the problems of incomplete combustion, serious heat waste, complex structure, and difficulty in adapting to gas composition fluctuations in the traditional flare system, and at the same time achieves the goals of energy conservation, emission reduction, and efficient energy utilization.

The utility model discloses an ignition torch with a variable air-fuel ratio, and relates to the technical field of industrial torches. Comprising an inner tube, a middle tube, a sleeve and an ignition electrode, first long holes are formed in the side face of the inner pipe in the axis direction, and a gas nozzle is arranged on the upper portion of the inner pipe. Second long holes are formed in the side face of the middle pipe in the axis direction. The sleeve is provided with a round hole for air to enter; the inner pipe penetrates into the middle pipe, the middle pipe penetrates into the sleeve, the inner pipe is detachably connected with the middle pipe, and the middle pipe is fixedly connected with the sleeve; the sleeve is provided with an ignition electrode; the inner pipe is connected with a gas pipeline; the air-fuel ratio of the ignition torch is adjusted to adapt to the change of fuel gas components, so that the ignition effect of the ignition torch is ensured; the problem that due to the fact that fuel gas components are different, an ignition torch cannot meet different fuel gas components at the same time, and ignition fails is solved.

A pre-vented soffit panel with an integrated screen to exclude wind-blown embers from entering the attic space. Vent holes are created in the soffit, and a screen is integrated therewith, in the factory or on a production line. The screen material is fire-resistant. The pre-vented soffit panel with integrated screen can then be packaged and shipped to a job or construction site, and installed instead of, or in place of, a prior-art soffit panel. The integrated soffit screen also prevents the intrusion of wind-blown snow and several types of insects. This integrated solution provides for more rapid and cost-effective job site installation without the need to perform costly retrofitting of metal vents into prior-art soffit panels.

The invention relates to the technical field of industrial automation control, in particular to a torch self-adaptive combustion optimization method and system. Acquiring multi-modal physical characteristic data of torch flame; dynamically constructing a torch combustion digital twinborn model by combining environment dynamic factor data, torch device state data and multi-mode physical characteristic data; predicting the transient concentration of key pollutants in the torch emissions based on a torch combustion digital twinborn model; according to the predicted transient concentration of the key pollutants, a hydrodynamic intervention strategy for the micro combustion area is generated; and based on a fluid dynamic intervention strategy, a fluid regulation and control execution mechanism arranged in the torch head is controlled, and transient fluid dynamic intervention is carried out on the microcosmic combustion area. The problems of insufficient combustion and high pollution emission of a traditional torch system can be solved.

The invention belongs to the technical field of ignition, and discloses a three-component pintle rotational flow torch igniter. According to the three-component pintle rotational flow torch igniter, liquid fuel is jetted through the central pintle rotational flow nozzle, and a gas oxidizing agent is jetted through the peripheral rotational flow nozzle. The liquid fuel from the pintle swirl nozzle moves in the radial direction, and the gas oxidizing agent from the swirl nozzle rotates in the axial direction, so that the interaction between the liquid fuel and the gas oxidizing agent is enhanced, the atomization quality is improved, and the ignition success rate is further improved. Besides, the flame temperature of the torch igniter is increased through secondary oxygen or air jetted from the body part of the torch igniter, and meanwhile, the wide-range adjustment of the flame temperature of the torch igniter is realized. The device is suitable for large combustion devices such as liquid rocket engines, gas generators and combustion heaters.

The utility model provides a flare gas recycling system. The flare gas recycling system comprises a flare gas liquid separation tank, a compressor unit, a flare gas water-sealed tank and a heating furnace, a flare gas inlet and a gas phase outlet are formed in the flare gas liquid separation tank, and the flare gas inlet is used for introducing flare gas; the gas phase outlet is respectively communicated with the compressor unit and the flare gas water-sealed tank; the flare gas is separated into a gas phase part and a liquid phase part by the flare gas liquid separation tank; the heating furnace is communicated with the compressor unit through a fuel gas pipeline, and the heating furnace is used for receiving the compressed gas phase part and taking the compressed gas phase part as fuel; the flare gas water-sealed tank is also communicated with an elevated flare; the flare gas water-sealed tank collects the escaping gas phase part and leads the escaping gas phase part to the elevated flare. The flare gas is recovered and then subjected to gas phase and liquid phase separation, and the compressor unit is additionally arranged to carry out pressure increasing treatment on the flare gas, so that stable air pressure in front of the heating furnace and stable operation of the heating furnace are ensured, and the gas is fully combusted and utilized in the heating furnace.

A torch assembly is configured to produce a flame and includes a body extending along a centerline with a first end and a second end opposite the first end. An ignitor assembly is disposed within the body to produce a flame. A burn tube extends from the second end of the body and is in fluid connection with the ignitor assembly. The burn tube includes a first portion extending from the body and a second portion connected to the first portion and angled relative to the first portion to define a bend therebetween for directing the flame out of the burn tube in a direction transverse to the centerline. A longitudinal cross section of the burn tube interior varies between the bend and the second end of the body for controlling a characteristic of the flame.

The utility model relates to a detachable economical torch which comprises a barrel body, one end of the barrel body is installed and fixed through a foundation bolt, the other end of the barrel body is provided with a burner assembly, the burner assembly is fixedly provided with an ignition barrel assembly, the ignition barrel assembly is connected with one end of a fuel gas valve set, and the fuel gas valve set is fixedly arranged on the barrel body. An air discharging inlet is formed in the cylinder body and is communicated with the combustor assembly; a thermocouple and an ignition rod are further fixedly arranged on the combustor assembly, the thermocouple is electrically connected with the local control box through a thermocouple cable, and the ignition rod is electrically connected with the ignition box through an ignition cable. The torch is high in integration level and convenient to disassemble, and can be automatically ignited at any time in an emptying state.

The present invention presents a method of assessing the quality of the burning of the gases in the flare and adjusting the vapor flow rate in a continuous way and with flexibility to integrate with different instrumentation topologies of the flare control system. The state of the flare flame is identified from an image set of the flame, classifying it into one of four: flame with excess vapor, optimized flame, flame with soot or images with insufficient information to classify them as one of the previous states of the flare flame. In addition, it is further able to quantify the height of the flame. The invention comprises the following components: flare, camera, image stream manager, edge computer, data historian, alert manager, information visualization panels, distributed digital control system, DDCS, and cloud storage and computing.

The invention discloses an emergency sampling and monitoring system and method for flue gas discharged by a torch, and relates to the technical field of flue gas collection and monitoring. A sampling control unit is installed on a detection positioning module in a sliding mode, the detection positioning module achieves movement of the sampling control unit through rotation, an infrared thermal imager is installed on a movable detection platform and used for detecting the smoke plume track, and a concentration detection unit is installed on the sampling control unit in a sliding mode and moves along the peripheral side of a torch. The PID sensors are used for detecting VOCs concentrations at different positions of smoke plume, the heat preservation collection box is connected with the vehicle-mounted analysis unit through a smoke tracing pipe, collection pipelines are arranged between the smoke collector and the concentration detection unit, each PID sensor corresponds to one collection pipeline, and the smoke collector collects smoke at an optimal sampling point into the heat preservation collection box through the collection pipelines. Through the pre-stored gas sampling monitoring mode, the influence on the smoke sampling monitoring process caused by the smoke plume track change can be effectively avoided.

Systems and devices for igniting a gas to be flared include: a body having an inlet and an outlet, the body defining a channel extending between the inlet and the outlet; an igniter operable to generate a spark at the outlet of the body; an actuator disposed in the channel, the actuator configured to harvest energy when the gas to be flared flows from the inlet to the outlet through the channel and transfer the energy to the igniter.