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67results about How to "Increase steam production" patented technology

Cooling water jacket of petroleum coke can-type calcine furnace

The invention discloses a petroleum coke pot typed calciner cooling water jacket, comprising a step-one heat exchanging device which is used for enclosing a high-temperature material passage; the step-one heat exchanging device comprises a ring-shaped upper container which is provided with a water outlet, a ring-shaped lower container which is provided with a water inlet, a plurality of heat exchanging pipes which are fixedly connected with the upper container and the lower container and communicated with each other respectively, a heat guiding baffle which is fixedly connected between two adjacent heat exchanging pipes; the high-temperature material passage which is enclosed by the step-one heat exchanging device is internally provided with a step-two heat exchanging device. The cooling water sleeve has good rigidity, and is not easy to generate thermal deformation; furthermore, the heat exchanging area is large and the cooling and heat exchanging effect is good; by increasing the step-two heat exchanging device, the uniformity of the temperature inside the whole passage is greatly improved, the temperature of the outgoing material is lowered from 300 DEG C to 150 DEG C; with the reduction of the temperature of the material, the service life of the material drainage valve is prolonged, and the malfunction rate of the material drainage system is reduced.
Owner:SHANDONG LIANXING ENERGY SAVING SERVICE

Control method for getting wind process for kiln hood waste heat boiler in dry cement residual heat utilization and apparatus thereof

InactiveCN101407382AStabilization and inlet air temperature and steam productionIncrease the inlet air temperature and steam productionClinker productionCement kilnEngineering
The invention relates to the fields of the recycle and application to electricity generation of waste gas and residual heat of a kiln head clinker cooler of a novel dry method cement production line. On the basis that at the kiln head cooler, the temperature of the cooled clinker is 600-200 DEG C of a cooling grate bed area and the discharging temperature of the cooler is ensured to meet the requirement, the invention controls and improves the temperature of hot air at the upper part of a clinker layer after heat exchange with the clinker, through utilizing first-discharging waste gas discharged to air and with temperature of 80-120 DEG C as cooling air which is corresponding to the area and used for cooling the clinker, effectively controlling the thickness of the clinker layer in the cooler and improving the temperature of the cooling air which is corresponding to the area and used for cooling the clinker. According to the temperature of hot air at the upper part of the corresponding clinker layer, the thickness of the clinker layer in the cooler and the temperature of the cooling air can be regulated in real time. The invention has the advantages of further stabilizing and improving the temperature of inlet air and steam production of residual heat boilers, stabilizing and improving generated energy of residual heat generation, and simultaneously improving the rate of multipurpose utilization of cement kiln residual heat resources.
Owner:昆明阳光基业股份有限公司

Revolving furnace, electric stove steel-smelting high-temperature gas cooling down heat-recovering steam producing energy conservation system device

The present invention relates to a steel-making high temperature gas cooling waste heat recycling steam producing energy saving system device for a converter and an electric oven. The present invention is characterized in that the device comprises a plurality of steam generators (1) which are connected in series and whose the gas circulating section is decreased in cascade type, an inlet interface (5) is arranged at one end of the steam generator (1), an outlet interface (7) is arranged at the other end, a heat transfer element (6) is arranged inside the steam generator (1), and the steam generator (1) is connected with a steam drum through each steam-water connecting pipe (4). The steam generator system waste heat steam producing energy saving device which is arranged in a high temperature chimney neck makes the gas temperature in the chimney neck decrease from 1000 degrees centigrade to 180 degrees centigrade to discharge, meeting the purposes of waste heat reuse and energy conservation. The present invention has the advantages that heat transfer efficiency is improved, each part of the process is independently arranged dispersedly, the equipment cubage is small, the disassembly is convenient, and the routine maintenance and the servicing and repair are convenient.
Owner:NANJING SHENGNUO HEAT PIPE

Coke oven raw gas high temperature segment heat high efficient recovering device

The invention relates to a coke oven raw gas high temperature segment heat high efficient recovering device. A vertical pipe sleeve pipe type quenching waste heat boiler is composed of a sleeve pipe type steam heat exchanger and a steam pocket. The air inlet in the top of the sleeve pipe type steam heat exchanger is connected to the air collection pipe in the top of a coke oven through a high temperature deduster. The water inlet of the steam pocket is connected to a desalting water tank though a low temperature heat exchanger, a boiler water pump, an oxygen remover, and a deoxidizing water pump in sequence. The steam outlet in the top of the steam pocket is connected to a low pressure steam user through a temperature reducing and pressure reducing device; or is connected to a high voltage generating user through a steam super-heater. The sewage outlet in the bottom of the sleeve pipe type steam heat exchanger is connected to a drain well through a periodic sewage discharge expander. The provided device can high efficiently recover the heat of the coke oven raw gas high temperature segment and generate high temperature high pressure saturated steam; thus high pressure overheated steam or low pressure saturated steam is produced, at the same time, condensation of polymers in equipment is reduced, the coking period is prolonged, the coke cleaning efficiency is improved, and the stable operation of the system is guaranteed.
Owner:ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC

Heat recovery system for high temperature flue gas at ammoxidation section

A heat recovery system for high temperature flue gases at an ammoxidation section, is used for preparing sodium nitrate/sodium nitrite. An ammoxidation furnace is connected with a waste heat boiler, the waste heat boiler is communicated with an external pipe by a valve 3, a desalinizing water tank is communicated with the waste heat boiler by the valve 1, a coal economizer is added between the waste heat boiler and an alkali absorption section, the coal economizer is communicated with the desalinizing water tank by a valve 2, a pneumatic regulating valve remotely controlled by a distributed control system, is connected between the coal economizer and the desalinizing water tank in series, and the pneumatic regulating valve and a manual regulating valve are connected in parallel. The coal economizer of the invention is used for supplementing water for a boiler for heating, which increases steam production amount, enhances a heat energy utilization rate, and can effectively implement purposes of energy saving and consumption reduction; the coal economizer is used to reduce a process gas temperature, indirectly raises a sodium nitrite/sodium nitrate content ratio value in an alkali absorption liquid in an alkali absorption section, and enables a tail gas content to reach 800mg/m3, and benefits for environmental protection; and the pneumatic regulating valve is mounted on the coal economizer, and is convenient for remote control by the distributed control system.
Owner:襄阳泽东化工集团股份有限公司

Cooling water jacket of petroleum coke can-type calcine furnace

The invention discloses a petroleum coke pot typed calciner cooling water jacket, comprising a step-one heat exchanging device which is used for enclosing a high-temperature material passage; the step-one heat exchanging device comprises a ring-shaped upper container which is provided with a water outlet, a ring-shaped lower container which is provided with a water inlet, a plurality of heat exchanging pipes which are fixedly connected with the upper container and the lower container and communicated with each other respectively, a heat guiding baffle which is fixedly connected between two adjacent heat exchanging pipes; the high-temperature material passage which is enclosed by the step-one heat exchanging device is internally provided with a step-two heat exchanging device. The cooling water sleeve has good rigidity, and is not easy to generate thermal deformation; furthermore, the heat exchanging area is large and the cooling and heat exchanging effect is good; by increasing the step-two heat exchanging device, the uniformity of the temperature inside the whole passage is greatly improved, the temperature of the outgoing material is lowered from 300 DEG C to 150 DEG C; with thereduction of the temperature of the material, the service life of the material drainage valve is prolonged, and the malfunction rate of the material drainage system is reduced.
Owner:SHANDONG LIANXING ENERGY SAVING SERVICE

Beryllium oxide generation preventing method for boilers of power plant

The invention discloses a beryllium oxide generation preventing method for boilers of a power plane, and the method can effectively avoid dry burning of heated surfaces. The method includes the following steps that firstly, a deaerator is heated, specifically, auxiliary steam is used for heating the deaerator, the heat source can increase the water temperature of the deaerator to 160 DEG C, and the temperature of a start-up separator outlet (or a steam pocket) of the corresponding boiler reaches 75 DEG C or above; secondly, feed water is heated, specifically, feed water heaters for starting of a unit are added through technical transformation or unit high-pressure heaters are directly selected, a steam source is taken from an adjacent unit and connected into the heaters, the feed water temperature is increased to a larger extent, the steam production amount is increased, the temperatures of the heated surfaces are greatly increased, the hearth temperature is increased, and the combustion condition in the ignition preliminary stage of the boilers is greatly improved; and thirdly, water is fed to the boilers till start-up separators encounter water, all drainage and vent valves of the boilers are closed, a steam turbine vacuum pump is started, and high-pressure bypass boilers and low-pressure bypass boilers are started and vacuumized.
Owner:CHANGSHA POWER STATION CO LTD OF HUNAN CHD

Propane dehydrogenation device and propane dehydrogenation method

The invention relates to a propane dehydrogenation device and a propane dehydrogenation method. The propane dehydrogenation device comprises a dehydrogenation reactor (1) and a heat exchanger (2), wherein a tube pass inlet (24) of the heat exchanger (2) is connected with a reaction raw material conveying pipeline (a); a tube pass outlet (25) of the heat exchanger (2) is connected with an inlet ofthe dehydrogenation reactor (1) through a heating furnace (3); an outlet of the dehydrogenation reactor (1) is connected with a reaction product conveying pipeline (b); the reaction product conveyingpipeline (b) is divided into two paths; a first path of reaction product conveying pipeline (b1) is connected with a shell pass inlet (22) of the heat exchanger (2) through a valve (5); a second pathof reaction product conveying pipeline (b2) is connected with the shell pass inlet (22) of the heat exchanger (2) through a steam generator (4); a shell pass outlet (23) of the heat exchanger (2) is connected with downstream equipment. The propane dehydrogenation device is low in investment and high in heat exchange efficiency, a bias problem occurred among multiple heat exchangers is effectivelyavoided, the stability of the propane dehydrogenation device, the yield of propylene and the steam output are improved, and an operation cycle is prolonged.
Owner:ZHENHAI PETROCHEM JIANAN ENG

Flame pressing type water tube boiler

The invention discloses a flame pressing type water tube boiler in the field of steam generation devices, which comprises a vertically arranged boiler body, tubes are vertically arranged in the boiler body, the tubes are arranged in a concentric annular array, three layers of tubes are arranged from inside to outside, a flame pressing plate is arranged in a circular cavity formed by the tubes on the inner layer, and a hearth is arranged below the flame pressing plate; a spiral coil pipe is also arranged on the periphery of the tube array in the boiler body; and smoke baffles are arranged between the tubes on the adjacent layers and between the tubes on the outer layer and the spiral coil pipe respectively, flow separation components are arranged between the tubes on the same layer and on the inner sides or the outer sides of the tubes on the same layer, a vertically reciprocating baffling channel is formed between the flow separation components and the smoke baffles in the space in the hearth, and the outermost side of the baffling channel is connected to a smoke outlet. The flame pressing type water tube boiler is small in water storage amount and large in steam production amount. The flame pressing type water tube boiler can be made into fire coal, fuel oil, natural gas or biomass energy boilers and can be applied to various places needing steam.
Owner:扬州大唐热能机械制造有限公司

Red coke transporting apparatus and red coke transporting method suitable for quenching coke

The invention belongs to the field of metallurgy, and relates to a red coke transporting apparatus and a red coke transporting method suitable for quenching coke. According to the red coke transporting apparatus, tracks are arranged on one side of a coke oven and parallel to the direction of the coke oven, a coke quenching vehicle rotation platform is arranged along the track direction, the upperportion of the coke quenching vehicle rotation platform is provided with tracks with the same spacing and the same type, a pit is arranged on one end of the coke quenching vehicle track and below theground perpendicular to the track direction, a dry quenching coke tank is arranged in the pit, the coke tank is positioned on a carrying vehicle, one end of the pit is connected to the end of the cokequenching vehicle track through a coke guide chute, and the other end of the pit is provided with a winch and a winding shaft frame. According to the present invention, the red coke is spread on thecoke receiving groove of the coke quenching vehicle after the red coke is pushed out of the carbonization chamber, the coke quenching vehicle walks along the tracks to the quenching coke tank position, the flipping mechanism under the coke receiving groove pushes the coke receiving groove to flip toward the dry quenching coke tank direction, and the red coke directly flips into the coke guide chute, and then enters the dry quenching coke tank, such that the red coke is pushed out of the coke oven and is transported to the dry quenching coke tank; and the apparatus and the method are especiallysuitable for the red coke transporting of the horizontal heat recovery coke oven using coke dry quenching.
Owner:SHANDONG PROVINCE METALLURGICAL ENG CO LTD

System of increasing steam productivity of low-temperature exhaust heat recovery in acid production from sulfur

The invention discloses a system of increasing steam productivity of low-temperature exhaust heat recovery in acid production from sulfur. The system includes: a high-temperature absorption column, asteam generator, and a dry absorption section, etc. The steam generator is arranged around a mixer to absorb heat generated therefrom for producing steam and outputs the steam via a pipeline; the dryabsorption section is connected to the high-temperature absorption column and the mixer and is used for absorbing SO3 gas and water in air to produce sulfuric acid; the sulfuric acid then is deliveredto a secondary sprinkling device of the high-temperature absorption column and a finish product acid output pipeline; the sulfuric acid diluted in the mixer is delivered to the dry absorption sectionby means of a primary sprinkling device in the high-temperature absorption column. In the application, the source of secondary sprinkling acid in the secondary sprinkling device in the high-temperature absorption column is changed, and a connection pipeline between the mixer and a dry acid trough in the dry absorption section is optimized, so that acid mixing mode in the dry absorption section ismodified. The system simplifies the structures of the devices and greatly improves the steam productivity in summer.
Owner:襄阳泽东化工集团股份有限公司
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