31results about How to "Reduce smoke temperature deviation" patented technology

A low-Nox combustion technology features that the combustion box is divided into primary combustion region, reduction region and burning off region from bottom to top. In the primary combustion region, the multi-layer horizontal coal powder combustion technique is used. In the reduction region the under-oxygen reduction technique is used. The burn0off air is fed into the burning off region. The jet direction of the secondary wind among each two burner layers is deflected clockwise by 10-15 deg. relative to the jet direction of primary wind and coal powder stream. The excessive coefficient of air in reduction region is 1.0. The horizontal direction of burn-off windjet is deflected anticlockwise by 5-10 deg. relative to the jet direction of primary wind. Its advantages are stable and uniform combustion, and low release of Nox.

The invention provides a multi-dimensional air staging low-NOx combustion system and an arrangement method. The stable combustion capability and the pulverized coal combustion efficiency of a boiler during the unit low-load operation stage are not taken into consideration in an existing staging NOx combustion method. During the unit low-load operation stage, if concentrated phase pulverized coal air flow deflects towards the fire-side water-cooled wall at wide angle, the problems that boiler combustion gets worse, slag is agglomerated on the water-cooled wall of the boiler and high-temperaturecorrosion becomes more severe due to reverse rotation of the boiler combustion tangential circle occur very easily. The multi-dimensional air staging low-NOx combustion system comprises main combustors and two-stage over- fire air combustors. The main combustors are arranged at the four corners of a boiler furnace (25) correspondingly. An included angle alpha formed between the central axis (22)of each main combustor and the water-cooled wall of the boiler furnace is 40-43 degrees. A set of secondary air nozzles and primary air nozzles arranged in a spaced mode are arranged on each main combustor.

The invention relates to a method for adjusting deviation of two sides of the reheating steam temperature of a four-corner tangential firing boiler by SOFA air doors. The method for adjusting the deviation of the two sides of the reheating steam temperature of the four-corner tangential firing boiler by the SOFA air doors comprises the steps that horizontal pendulum angles of the SOFA air doors are adjusted; when the deviation of two sides of the reheating steam temperature is removed, vertical pendulum angles of the SOFA air doors are no longer adjusted; when the deviation of two sides of thereheating steam temperature is not removed, the vertical pendulum angles of the SOFA air doors are adjusted; and when the vertical pendulum angles of the SOFA air doors are adjusted, firstly, the vertical pendulum angles of a second SOFA air door and a third SOFA air door are adjusted obliquely upwards, and then, the vertical pendulum angles of a first SOFA air door and a fourth SOFA air door areadjusted to horizontal positions. The adjustment of the reheating steam temperature and temperature-decreased water flow is realized through the cooperative cooperation of the horizontal pendulum angles and the vertical pendulum angles of the SOFA air door, through the nonsynchronous adjustment of the horizontal pendulum angles and the vertical pendulum angles, the deviation of two sides of smoketemperature of the four-corner tangential firing boiler is rapidly reduced, the high-temperature point of the reheater pipe wall is reduced, the problems of large deviation of a reheater outlet stream temperature and the unbalanced temperature-decreased water flow on two sides are solved, finally, the average stream temperature of the reheater outlet is improved, and the temperature-decreased water flow of the reheater is reduced.

The invention relates to a coal-fired boiler secondary air valve baffle control method based on burner heat loads. The secondary air valve aperture is set according to different burning characteristics of burners on all layers, the secondary air interlayer distribution is controlled, and real-time matching control over secondary air distribution of burner areas and the heat loads of the burners on all layers is carried out. Compared with the prior art, the coal-fired boiler secondary air valve baffle control method has the advantages that burning conditions of the different heat loads of the burners can be met, the boiler burning economical efficiency is improved, the NOx emission is reduced, and the smoke temperature deviation is reduced.

The invention provides hexagonal or octagonal tangential arrangement of anthracite burning single-fireball direct-flow combustors, which is characterized in that: two groups of combustors are arranged on each water-cooling wall or two groups of combustors are arranged on two opposite water-cooling walls of a hearth respectively and a group of combustors are arranged on the other two opposite water-cooling walls respectively, each group of combustors are at least divided into a small group; and each small group of combustors are vertically provided with at least two primary air pulverized nozzles and three secondary air pulverized nozzles at intervals. Each coal mill is connected with eight or six primary air pulverized nozzles which have the same level with that of the coal mill. The start and stop of each coal mill affect the running of the eight or six primary air pulverized nozzles which are on the same layer. The hexagonal or octagonal tangential arrangement of the anthracite burning single-fireball direct-flow combustors can decrease the number of the air pulverized nozzles in a single group of combustors on the premise of meeting the requirements of the thermal power of a single air pulverized nozzle and the number of the total air pulverized nozzles, allows the thermal load qHr of a wall in a combustor area to be relatively high, and guarantees the timely ignition of anpulverized anthracite flow and low-load combustion of a boiler without oil.

The invention belongs to a method for the on-line monitoring and alarming of a convection heating face flue gas temperature field of a power station boiler, which comprises the steps of calculating the average value of temperatures of furnace inner walls on inlet and outlet planes according to monitoring values of the temperatures of the furnace inner walls; additionally arranging flue gas temperature monitoring points at two sides; amending a flue gas average temperature; calculating the flue gas temperature of each point in the inlet and outlet planes of the heating faces, and the flue gas temperature of various planes vertical to the inlet and outlet planes of the heating faces; automatically generating a planar dynamic flue gas temperature colorful distribution diagram; and displaying in real time and providing site conditions and timely adjusting work conditions. The method disclosed by the invention realizes the accurate data monitoring and corresponding and visual diagram distribution display of flue gas temperature fields in the inlet and outlet planes and various longitudinal and horizontal planes vertical to the inlet and outlet planes of each convection heating face of superheater and reheater pipeline systems, provides direct data support for adjusting the burning work condition of the operation site of the power station boiler, and realizes the safe and economic operation of the convection heating faces of the superheater and reheater pipeline systems of the power station boiler.