公开(公告)号：US3758037A

公开(公告)日：1973-09-11

申请号：US3758037D

申请日：1971-10-04

Applicant: TEXACO DEVELOPMENT CORP

Inventor： MARION CH ,  REYNOLDS B

IPC: C01B3/36 ,  C10G9/00 ,  F23D11/38 ,  F23D14/22 ,  F23D14/32 ,  F23D14/48 ,  F23D17/00 ,  B05B15/00

CPC classification number: F23D14/32 ,  C01B3/363 ,  F23D14/22 ,  Y02E20/344

Abstract: A partial oxidation burner and process for the manufacture of synthesis gas, reducing gas and other gas mixtures substantially comprising H2 and CO. A hydrocarbon, oxygen-rich gas and, optionally, H2O or some other temperature moderator are introduced into the reaction zone of a synthesis gas generator in which, by partial oxidation at an autogenous temperature in the range of about 1700* to 3500*F. and a pressure in the range of about 1 to 250 atmospheres, said synthesis, fuel, or reducing gas is produced. For example, a hydrocarbon is introduced into the reaction zone by way of the inner assembly of a novel multitube burner, and a mixture of oxygen-rich gas and steam is passed through a coaxial conduit disposed about the outside of said inner assembly. Said inner asembly comprises a central conduit of circular cross-section, having a plurality of parallel open-ended tubes extending downstream from the exit end of said central conduit and in communication therewith. The tubes terminate in a surrounding nozzle, which is the exit end of the coazial outer conduit.

Abstract translation: 一种部分氧化燃烧器和用于制造基本上包含H 2和CO的合成气，还原性气体和其它气体混合物的方法。将烃，富氧气体和任选的H 2 O或一些其它温度调节剂引入到 合成气体发生器，其中通过在自发温度在约1700°至3500°F的范围内的部分氧化和约1至250大气压的范围内的压力产生所述合成，燃料或还原性气体。 例如，通过新型多管燃烧器的内部组件将烃引入反应区，富氧气体和蒸汽的混合物通过设置在所述内部组件外侧的同轴导管。 所述内部组件包括圆形横截面的中心导管，其具有从所述中心导管的出口端的下游延伸并与其连通的多个平行的开放式管。 管终止于周围喷嘴，其是同侧管外管的出口端。

公开(公告)号：US3847564A

公开(公告)日：1974-11-12

申请号：US30806772

申请日：1972-11-20

Applicant: TEXACO DEVELOPMENT CORP

Inventor： MARION C ,  REYNOLDS B

IPC: C01B3/36 ,  C07C1/02

CPC classification number: C01B3/363 ,  F23D11/36 ,  F23D2214/00 ,  F23D2900/00006 ,  F23L7/005

Abstract: This disclosure pertains to a triple-orifice burner and process for atomizing a stream of normally liquid hydrocarbon with a separate stream of free-oxygen-containing gas a finite distance downstream from the tip of the burner and for simultaneously enveloping the mixed streams with a separate stream of temperature-moderating gas so that none of the three streams comes into contact with any other gas with which it is combustible until it reaches a distance downstream from the tips of the burner orifices beyond that close enough to cause appreciable deterioration of the tips when reaction takes place in a free-flow partial oxidation gas generator at a temperature in the range of about 1,200* to 3500*F. and at a pressure in the range of about 1 to 275 atmospheres to produce a gaseous mixture comprising principally H2 and CO, e.g., synthesis gas, reducing gas, or fuel gas. While the liquid hydrocarbon is passed through the burner at a velocity in the range of about 10 to 100 feet per second, both the stream of free-oxygen-containing gas and the stream of temperature-moderating gas may be passed through the burner at velocities up to sonic velocity when it is desired to offset the effects of variable back pressure in the gas generator. The burner comprises three coaxial concentric nozzles whose tips are recessed from the downstream tip of the burner and which discharge into a single unobstructed coaxial central outwardlydiverging passage with an annular face of convex configuration at the extremity of the downstream tip of the burner. An imaginary plane tangent to said annular face at its outermost extremity is normal to the burner axis. The three nozzles provide, respectively, a central passage with a circular opening for discharging a stream of liquid hydrocarbon, an intermediate converging annular passage for discharging a stream of freeoxygen-containing gas, and an outer converging annular passage for discharging a stream of temperature-moderating gas, such as steam. An annular coolant chamber is disposed about the outside periphery of said outer discharge passage and downstream burner tip.

Abstract translation: 本公开涉及一种三孔燃烧器和用于使来自燃烧器尖端下游有限距离的独立的含游离氧气流的雾化正常液体烃的流程，并且同时用单独的 温度调节气体流，使得三个流中的任何一个都不会与其可燃烧的任何其它气体接触，直到其到达燃烧器孔口的顶部的下游距离足够远以致引起明显的尖端劣化 反应发生在自由流动的部分氧化气体发生器中，温度范围为约1200°至3500°F，压力范围为约1至275大气压，以产生主要包含H 2和CO ，例如合成气，还原气体或燃料气体。 当液体烃以约10至100英尺/秒的速度通过燃烧器时，含游离氧的气体流和温度调节气体流可以以速度通过燃烧器 当需要抵消气体发生器中可变背压的影响时，达到声速。

公开(公告)号：US3743606A

公开(公告)日：1973-07-03

申请号：US3743606D

申请日：1970-01-23

Applicant: TEXACO DEVELOPMENT CORP

Inventor： MARION C ,  REYNOLDS B

IPC: C01B3/36 ,  C07C1/02

CPC classification number: C01B3/363

Abstract: MANUFACTURE OF SYNTHEIS GAS BY PARTIAL OXIDATION OF A NORMALLY LIQUID HYDROCARBON BY FEEDING INTO THE REACTION ZONE A RELATIVELY LOW VELOCITY STREAM OF LIQUID HYDROCARBON AND A STREAM OF OXYGEN-CONTAINING GAS THRU SEPARATE CENTRAL NOZZLES OF A TRIPLE ORIFICE BURNER IN SUCH A MANNER AS TO EFECT ATOMIZATION OF THE OIL DOWNSTREAM OF THE BURNER, THESE STREAMS BEING ENCLOSED IN A THIRD, OUTER ANNULAR STREAM OF MODERATOR GAS, SUCH AS STEAM, SO THAT NONE OF THE THREE STREAMS COMES INTO CONTACT WITH ANY OTHER GAS WITH WHICH IT IS COMBUSTIBLE UNTIL IT REACHES A DISTANCE DOWNSTREAM FROM THE BURNER TIPS BEYOND THAT CLOSE ENOUGH TO CAUSE APPRECIABLE DETERIORATION.

公开(公告)号：US3723345A

公开(公告)日：1973-03-27

申请号：US3723345D

申请日：1969-11-21

Applicant: TEXACO DEVELOPMENT CORP

Inventor： REYNOLDS B

IPC: C01B32/40 ,  C07C1/02

CPC classification number: C01B32/40 ,  Y02P20/129

Abstract: SYNTHESIS GAS, I.E., A MIXTURE OF CARBON MONOXIDE AND HYDROGEN IS PRODUCED BY DIRECT PARTIAL OXIDATION OF A HYDROCARBON FUEL WITH OXYGEN FOLLOWED BY NON-CATALYTIC REACTION WITH STEAM AT A TEMPERATURE OF AT LEAST 1500* F. AND PREFERABLY IN THE RANGE OF ABOUT 1700 TO 2800* F. IN ONE OR MORE REACTION ZONES.

公开(公告)号：US3723344A

公开(公告)日：1973-03-27

申请号：US3723344D

申请日：1969-11-21

Applicant: TEXACO DEVELOPMENT CORP

Inventor： REYNOLDS B

IPC: C01B3/16 ,  C01B3/22 ,  C01B3/36 ,  C01B32/40 ,  C07C1/02

CPC classification number: C01B3/36 ,  C01B3/16 ,  C01B3/22 ,  C01B32/40

Abstract: Oxo-synthesis gas, i.e. a mixture of carbon monoxide and hydrogen containing substantially equal volumes of hydrogen and carbon monoxide is produced by direct partial oxidation of a hydrocarbon fuel with oxygen followed by noncatalytic reaction with carbon dioxide at a temperature of at least 1,500*F., and preferably in the range of about 1,700* to 2,800*F. in one or more reaction zones.

Abstract translation: 通过用氧气直接部分氧化烃燃料，然后在至少1500°F的温度下与二氧化碳进行非催化反应，产生氧合成气，即一氧化碳和含有基本相同体积氢气和一氧化碳的氢气的混合物 优选在一个或多个反应区中在约1700至2800°F的范围内。