摘要:
An ethylene cracking furnace mainly comprising: a radiant section (1), a convection section (2), and TLEs (Transfer Line Exchangers) (8), wherein said radiant section (1) is provided with at least one firebox (3) with its bottom provided with a plurality of burners (9), said plurality of burners (9) comprises a first, a second, a third and a fourth rows of burners arranged in sequence and parallel with each other; said firebox (3) is provided with a first group of radiant coils and a second group of radiant coils, both said first group of radiant coils and said second group of radiant coils are arranged in two rows, such that said firebox (3) is provided with four rows of radiant tubes in total. The present invention realizes large scale cracking furnaces which take up less space and require less investment as compared with other cracking furnaces having the same dimension. Respective embodiments provided in the present invention further provide more beneficial technical effect.
摘要:
Systems for dehydrogenating an alkane are provided. An exemplary system includes a furnace and further includes alkane heating chambers, regeneration mixture heating chambers, and two groups of reaction chambers, all located within the furnace. The alkane heating chambers and regeneration mixture heating chambers can preheat an alkane feed and a regeneration mixture feed, respectively. The two groups of reaction chambers can be switchably coupled to an alkane feed and a regeneration mixture feed such that an alkane can flow through one group of reaction chambers while a regeneration mixture flows through the other group of reaction chambers. Processes for dehydrogenating an alkane are also provided.
摘要:
Flames (30) generated in a furnace (1), having at one end (50) a plurality of fuel conduits (21) in spaced relation to a plurality of oxidant conduits (11), to heat reaction chambers (80) extending the length of the furnace, are straightened by limiting the combined horizontally projected turbulent free-jet area defined by the oxidant conduit outlets at 30% of the average distance from said one end (50) to the opposite end (60) of the furnace to between 10% and 105% of the horizontally projected area of said one end (50). The invention has particular application to steam methane reformers and ethylene cracking furnaces.
摘要:
A method of operating a pyrolysis heater for reduced emissions of NO x and carbon monoxide. One or more wall burners 20, typically premix burners, are operated with more excess oxidant gas than one or more of the floor or hearth burners 10, which are typically non-premix burners. The invention takes advantage of different NO x emissions characteristics from different types of burners.
摘要:
Apparatus and methods suitable for recovery of heat from hot flue gases are presented comprising primary heat transfer means (2) for exchanging heat between a hot flue gas (8) and an intermediate fluid (10) to create a hot intermediate fluid from an originally cold intermediate fluid; one or more oxidant-fuel burners (6) which create the main flow of hot flue gas, and transport means (4) for transporting the hot intermediate fluid to the heat exchanger means (20). The apparatus and method of the invention solve the problem of recovery of heat from dirty, toxic, or erosive flue gases.
摘要:
A method for operating a furnace (32) comprising generating NOx with burners (13,20) at a value exceeding the equilibrium value by combustion at a distance from the flue (34) and generating NOx with burners (1,12) at a lesser value, preferably at a value below the equilibrium value, by combustion close to the flue (34).
摘要:
The invention relates to a process for melting a charge by means of oxy-fuel combustion burners in a furnace (1) that includes at least one upstream flue gas outlet (3), in which furnace, in the charge melting zone: the burners (41-44) placed close to the upstream flue gas outlet burn a liquid fuel; and at least one of the burners (51-54) placed far from the upstream flue gas outlet burns a gaseous fuel.