CN110617466A - Supercritical hydrothermal combustion type steam generator for ultra-deep underground heavy oil thermal recovery - Google Patents
Supercritical hydrothermal combustion type steam generator for ultra-deep underground heavy oil thermal recovery Download PDFInfo
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- 238000002485 combustion reaction Methods 0.000 title claims abstract description 71
- 239000000295 fuel oil Substances 0.000 title claims abstract description 34
- 238000011084 recovery Methods 0.000 title claims abstract description 24
- 239000000446 fuel Substances 0.000 claims abstract description 44
- 239000007800 oxidant agent Substances 0.000 claims abstract description 42
- 230000001590 oxidative effect Effects 0.000 claims abstract description 40
- 239000000498 cooling water Substances 0.000 claims abstract description 39
- 230000009977 dual effect Effects 0.000 claims description 15
- 238000002156 mixing Methods 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims description 3
- 238000000889 atomisation Methods 0.000 claims description 2
- 239000003921 oil Substances 0.000 abstract description 12
- 239000007795 chemical reaction product Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- 238000005485 electric heating Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000005065 mining Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910052581 Si3N4 Inorganic materials 0.000 description 2
- 238000010795 Steam Flooding Methods 0.000 description 2
- 238000010796 Steam-assisted gravity drainage Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 229910052755 nonmetal Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000010793 Steam injection (oil industry) Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- -1 cermets Chemical compound 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
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- 150000002843 nonmetals Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
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- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/02—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using burners
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
- E21B43/243—Combustion in situ
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B3/00—Other methods of steam generation; Steam boilers not provided for in other groups of this subclass
- F22B3/08—Other methods of steam generation; Steam boilers not provided for in other groups of this subclass at critical or supercritical pressure values
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- Engineering & Computer Science (AREA)
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- Life Sciences & Earth Sciences (AREA)
- Mining & Mineral Resources (AREA)
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- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Spray-Type Burners (AREA)
Abstract
本发明公开了一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,包括发生器头部、发生器上部和发生器下部三部分。发生器头部上装有保证超临界水热燃烧反应发生的电加热棒;发生器上部包括一次燃烧室与二次燃烧室以保证燃料与氧化剂的充分超临界水热燃烧反应;发生器下部的喷头与渐缩口保证了反应产物的参数符合油田稠油开采的要求;发生器内的冷却水用于保证发生器不超温以保护发生器安全运行。本装置降低了稠油开采成本,提高热量利用效率,阻止了污染物的排放,实现了深层及海上油藏的高效开采。
The invention discloses a supercritical hydrothermal combustion type steam generator for thermal recovery of heavy oil in an ultra-deep well, comprising three parts: a generator head, a generator upper part and a generator lower part. The head of the generator is equipped with an electric heating rod to ensure the occurrence of supercritical hydrothermal combustion reaction; the upper part of the generator includes a primary combustion chamber and a secondary combustion chamber to ensure sufficient supercritical hydrothermal combustion reaction of fuel and oxidant; the nozzle at the lower part of the generator And the tapering port ensures that the parameters of the reaction product meet the requirements of heavy oil production in the oil field; the cooling water in the generator is used to ensure that the generator does not overheat to protect the safe operation of the generator. The device reduces the cost of heavy oil exploitation, improves heat utilization efficiency, prevents the discharge of pollutants, and realizes efficient exploitation of deep and offshore oil reservoirs.
Description
技术领域technical field
本发明属于稠油开采与超临界水技术领域,涉及一种蒸汽发生器,特别涉及一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器。The invention belongs to the technical field of heavy oil exploitation and supercritical water, and relates to a steam generator, in particular to a supercritical hydrothermal combustion steam generator used for thermal recovery of heavy oil in an ultra-deep well.
背景技术Background technique
超临界水(Supercritical Water,简称SCW)是指温度和压力均高于其临界点(T=374.15℃,P=22.12MPa)的特殊状态的水。在该状态下,水中只有少量的氢键存在,介电常数近似于有机溶剂,具有低的粘度和高的扩散系数。使有机物、氧气能按任意比例与超临界水互溶,从而使非均相反应变为均相反应,大大减少了物质之间的传质、传热阻力。Supercritical Water (SCW for short) refers to water in a special state whose temperature and pressure are both higher than its critical point (T=374.15°C, P=22.12MPa). In this state, only a small amount of hydrogen bonds exist in water, the dielectric constant is close to that of organic solvents, and it has low viscosity and high diffusion coefficient. Make organic matter and oxygen miscible with supercritical water in any proportion, so that the heterogeneous reaction becomes a homogeneous reaction, and the mass transfer and heat transfer resistance between substances are greatly reduced.
超临界水热燃烧(Supercritical Hydrothermal Combustion,简称SCHC)技术就是指燃料与氧化剂在超临界水环境中发生剧烈氧化反应,产生水热火焰(HydrothermalFlame)的一种新型燃烧方式,与常规燃烧技术相比,超临界水热燃烧技术具有燃烧核心温度较低,反应产物清洁,反应器很小等显著的优越性。Supercritical Hydrothermal Combustion (SCHC) technology refers to a new type of combustion method in which fuel and oxidant undergo violent oxidation reactions in a supercritical water environment to produce a hydrothermal flame (Hydrothermal Flame). Compared with conventional combustion technologies , Supercritical hydrothermal combustion technology has significant advantages such as low combustion core temperature, clean reaction products, and small reactor.
目前油田稠油的开采方法主要是在地面利用注汽锅炉产生蒸汽,注入井下结合蒸汽吞吐、蒸汽驱和蒸汽辅助重力泄油三种稠油热采技术开采稠油,以上方式主要存在以下瓶颈:地面蒸汽发生器占地面积大,无法布置于空间受限的海上石油开采平台,限制了海上稠油的开采;热损失大。地面蒸汽发生器的排烟损失约20%,地面输气管线热损失约15%,注入井筒热损失每千米约10%,整体热效率低;注气锅炉不可避免产生包含SOx与NOx的排烟会造成环境的污染;可采油藏深度受限,已发现的稠油油藏中,储层深度大于1700m的稠油储量约占已探明储量的40%。除蒸汽吞吐的应用深度达到1800米,采收率较高的蒸汽驱和蒸汽辅助重力泄油技术主要应用深度在1200米以内的油藏中。At present, heavy oil production methods in oilfields mainly use steam injection boilers on the ground to generate steam, which is injected downhole and combined with steam huff and puff, steam flooding and steam-assisted gravity drainage to recover heavy oil. The above methods mainly have the following bottlenecks: Ground steam generators occupy a large area and cannot be arranged on offshore oil exploration platforms with limited space, which limits the exploitation of heavy oil at sea; the heat loss is large. The exhaust gas loss of the surface steam generator is about 20%, the heat loss of the surface gas pipeline is about 15%, the heat loss of the injection wellbore is about 10% per kilometer, and the overall thermal efficiency is low; the gas injection boiler inevitably produces exhaust gas containing SOx and NOx It will cause environmental pollution; the depth of recoverable oil reservoirs is limited. Among the discovered heavy oil reservoirs, the reserves of heavy oil with a reservoir depth greater than 1700m account for about 40% of the proven reserves. In addition to the application depth of steam huff and puff up to 1800 meters, steam flooding and steam-assisted gravity drainage technology with high recovery rate are mainly applied in oil reservoirs with a depth of less than 1200 meters.
发明内容Contents of the invention
为了克服上述现有技术的缺点,解决现有注气锅炉产蒸汽开采稠油技术存在的巨大热损失、环境污染、开采成本高于开采深度有限等问题,本发明的目的在于提供一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,可直接在井下进行点火燃烧产生蒸汽与二氧化碳,降低常规地面产生蒸汽运输等热损失造成的高额成本,且反应器相对注气锅炉很小可降低大量材料成本及土地成本,并能实现压力自动调节成井下稠油热采所需的压力,还可避免注气锅炉排烟造成的环境污染,最终实现常规技术无法开采的超深油藏资源的开采工作。In order to overcome the shortcomings of the above-mentioned prior art, and solve the problems of huge heat loss, environmental pollution, mining cost higher than the limited mining depth and other problems existing in the existing gas injection boiler steam production technology for mining heavy oil, the purpose of the present invention is to provide a method for The supercritical hydrothermal combustion steam generator for thermal recovery of heavy oil in ultra-deep wells can be ignited and burned directly in the well to generate steam and carbon dioxide, reducing the high cost of heat loss caused by conventional ground-generated steam transportation, and the reactor is relatively injected The small size of the gas boiler can reduce a lot of material costs and land costs, and can automatically adjust the pressure to the pressure required for the thermal recovery of heavy oil in the well. Exploitation of ultra-deep oil reservoir resources.
为了实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:
一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,包括依次连接装配的发生器头部18、发生器上部19和发生器下部25,所述发生器头部18为端盖结构,其上设置有喷嘴口5,喷嘴口5中装有贯穿发生器头部18的喷嘴,所述喷嘴包括喷嘴内胆3、喷嘴外壳4和点火棒1,喷嘴内胆3侧壁开有一次燃料入口2,底端开有若干雾化喷口,点火棒1内插入喷嘴内胆3,喷嘴外壳4上部设有一次氧化剂入口15,喷嘴外壳4下方外部为喷嘴单螺旋结构。A supercritical hydrothermal combustion steam generator for thermal recovery of heavy oil in an ultra-deep well, comprising a generator head 18, a generator upper part 19 and a generator lower part 25 connected and assembled in sequence, the generator head 18 It is an end cover structure, on which a nozzle opening 5 is arranged, and a nozzle passing through the generator head 18 is installed in the nozzle opening 5. The nozzle includes a nozzle liner 3, a nozzle shell 4 and an ignition rod 1, and the nozzle liner 3 sides There is a primary fuel inlet 2 on the wall, several atomizing nozzles on the bottom, the ignition rod 1 is inserted into the nozzle liner 3, the upper part of the nozzle shell 4 is provided with a primary oxidant inlet 15, and the outside of the nozzle shell 4 is a nozzle single spiral structure.
所述发生器上部19的内部区域由上方的一次燃烧室10和下方的二次燃烧室11通过喉口组件23连通构成,二次燃烧室11的下方连接位于发生器下部25的喷头13,其中所述雾化喷口和喷嘴单螺旋结构均处于一次燃烧室10的上部。The inner area of the upper part 19 of the generator is formed by connecting the primary combustion chamber 10 above and the secondary combustion chamber 11 below through the throat assembly 23, and the nozzle 13 located at the lower part 25 of the generator is connected to the bottom of the secondary combustion chamber 11, wherein Both the atomizing nozzle and the single spiral structure of the nozzle are located at the upper part of the primary combustion chamber 10 .
所述发生器头部18上设有与一次燃烧室10连通的测压口一7、火焰检测口6和测温口一16,所述发生器上部19或发生器下部25设置有连通二次燃烧室11的测温口二24,所述发生器下部25设置有连通喷头13下方区域的测压口二14和测温口三26。The generator head 18 is provided with a pressure measuring port 17, a flame detection port 6 and a temperature measuring port 16 communicating with the primary combustion chamber 10, and the generator upper part 19 or the generator lower part 25 is provided with a communication secondary The temperature measuring port 2 24 of the combustion chamber 11 and the lower part 25 of the generator are provided with a pressure measuring port 2 14 and a temperature measuring port 3 26 communicating with the area below the nozzle 13 .
所述的喷头13上开有若干与水平面成45-80°的斜向下的喷口。Described shower head 13 has some obliquely downward spouts of 45-80° with the horizontal plane.
所述一次燃烧室10由耐火组件20环绕而成,所述的耐火组件20材料包括但不限于碳化硅、金属陶瓷、氮化硅等市面上可购买的一种或多种无机金属或非金属材料。The primary combustion chamber 10 is surrounded by a refractory component 20, and the material of the refractory component 20 includes, but is not limited to, one or more inorganic metals or non-metals available on the market such as silicon carbide, cermets, and silicon nitride. Material.
所述发生器上部19的侧壁设有二次燃料/氧化剂双通道22,所述发生器头部18上设有与二次燃料/氧化剂双通道22连通的二次燃料入口8和二次氧化剂入口17,所述二次燃料/氧化剂双通道22下端向内开有若干排倾斜向下的与二次燃烧室11连通的二次燃料/氧化剂混合出孔。The side wall of the upper part 19 of the generator is provided with a secondary fuel/oxidant dual channel 22, and the generator head 18 is provided with a secondary fuel inlet 8 and a secondary oxidant which communicate with the secondary fuel/oxidant dual channel 22 Inlet 17, the lower end of the secondary fuel/oxidant dual channel 22 is provided with several rows of secondary fuel/oxidant mixing outlets that are inclined downward and communicate with the secondary combustion chamber 11.
所述喷头13设置在发生器下部25内,所述发生器上部19的侧壁设有冷却水上通道21,冷却水上通道21位于二次燃料/氧化剂双通道22外侧,所述发生器头部18上设有与冷却水上通道21连通的冷却水入口9,所述发生器下部25的上方侧壁设有与冷却水上通道21相连通的冷却水下通道12,所述冷却水下通道12下方开有连接喷头13的冷却水出口。The nozzle 13 is arranged in the lower part 25 of the generator, and the side wall of the upper part 19 of the generator is provided with a cooling water channel 21, and the cooling water channel 21 is located outside the secondary fuel/oxidant dual channel 22, and the generator head 18 A cooling water inlet 9 communicating with the cooling water upper channel 21 is provided on the top, and a cooling water lower channel 12 communicating with the cooling water upper channel 21 is provided on the upper side wall of the lower part 25 of the generator. There is a cooling water outlet connected to the spray nozzle 13.
所述二次燃料/氧化剂双通道22为双螺旋下降结构,所述冷却水上通道21和冷却水下通道12为单螺旋下降结构。The secondary fuel/oxidant double channel 22 is a double spiral descending structure, and the cooling water upper channel 21 and the cooling water lower channel 12 are a single spiral descending structure.
所述二次燃料/氧化剂双通道22、冷却水上通道21和冷却水下通道12的螺旋平面均与水平面成10-45°,所述二次燃料/氧化剂混合出孔与水平面成45-80°。The spiral planes of the secondary fuel/oxidant double channel 22, the cooling water upper channel 21 and the cooling underwater channel 12 are all at 10-45° to the horizontal plane, and the secondary fuel/oxidant mixing outlet is at 45-80° to the horizontal plane .
所述发生器下部25底端整体为收缩喷管结构。The bottom end of the lower part 25 of the generator is a shrinking nozzle structure as a whole.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
(1)本发明公开的一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,在井下利用超临界水热燃烧技术产生蒸汽可以避免蒸汽锅炉的排烟与输汽管线所产生的45%以上的热损失,提高了整体的热效率,且该装置结构紧凑小巧,能够放置井下,使得产生蒸汽的过程不必在地面上使用庞大的注气锅炉产生,有效降低了投资成本和土地成本,从而提高了系统的经济性。(1) The invention discloses a supercritical hydrothermal combustion steam generator for thermal recovery of ultra-deep downhole heavy oil, which can avoid smoke exhaust and steam transportation of steam boilers by using supercritical hydrothermal combustion technology to generate steam underground More than 45% of the heat loss generated by the pipeline improves the overall thermal efficiency, and the device is compact in structure and can be placed underground, so that the process of generating steam does not need to be generated on the ground using a huge gas injection boiler, effectively reducing investment costs and land costs, thereby improving the economics of the system.
(2)本发明公开的一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,在井下利用超临界水热燃烧技术产生蒸汽,产物全部注入井下,不会往大气中排放注气锅炉不可避免的有毒排烟SOx以及NOx,保护了环境。(2) The invention discloses a supercritical hydrothermal combustion type steam generator for thermal recovery of ultra-deep downhole heavy oil. The supercritical hydrothermal combustion technology is used to generate steam in the downhole, and the products are all injected into the downhole without going to the atmosphere. The inevitable toxic exhaust SOx and NOx of medium-emission gas injection boilers protect the environment.
(3)本发明公开的一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,不受井深限制,可用于常规采油工艺难以利用的深层油藏、超深层油藏以及海上油藏,提高了油田油藏的使用率。(3) A supercritical hydrothermal combustion type steam generator for thermal recovery of ultra-deep downhole heavy oil disclosed by the present invention is not limited by well depth, and can be used in deep oil reservoirs and ultra-deep oil reservoirs that are difficult to utilize by conventional oil recovery techniques As well as offshore reservoirs, improving the utilization rate of oilfield reservoirs.
因此,本发明公开的一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,降低了稠油开采成本、提高热量利用效率、减少了污染物的排放、不受开采井深限制、实现了深层及海上油藏的高效开采。Therefore, the present invention discloses a supercritical hydrothermal combustion steam generator for thermal recovery of heavy oil in ultra-deep wells, which reduces the cost of heavy oil production, improves heat utilization efficiency, reduces pollutant discharge, and is not subject to exploitation. The well depth is limited, and the efficient exploitation of deep and offshore oil reservoirs is realized.
附图说明Description of drawings
图1为本发明装置的结构示意图。Fig. 1 is a structural schematic diagram of the device of the present invention.
其中,1为点火棒,2为一次燃料入口,3为喷嘴内胆,4为喷嘴外壳,5为喷嘴口,6为火焰检测器口,7为测压口,8为二次燃料入口,9为冷却水入口,10为一次燃烧室,11为二次燃烧室,12为冷却水下通道,13为喷头,14为测压口,15为一次氧化剂入口,16为测温口,17为二次氧化剂入口,18为发生器头部,19为发生器上部,20为耐火材料,21为冷却水上通道,22为二次燃料/氧化剂双通道,23为喉口组件,24为测温口,25为发生器下部,26为测温口。Among them, 1 is the ignition rod, 2 is the primary fuel inlet, 3 is the nozzle inner tank, 4 is the nozzle shell, 5 is the nozzle mouth, 6 is the flame detector mouth, 7 is the pressure measuring port, 8 is the secondary fuel inlet, 9 10 is the primary combustion chamber, 11 is the secondary combustion chamber, 12 is the cooling water channel, 13 is the nozzle, 14 is the pressure measuring port, 15 is the primary oxidant inlet, 16 is the temperature measuring port, 17 is the secondary The secondary oxidant inlet, 18 is the generator head, 19 is the upper part of the generator, 20 is the refractory material, 21 is the cooling water channel, 22 is the secondary fuel/oxidant dual channel, 23 is the throat assembly, 24 is the temperature measuring port, 25 is the lower part of the generator, and 26 is the temperature measuring port.
具体实施方式Detailed ways
下面结合附图和实施例详细说明本发明的实施方式。The implementation of the present invention will be described in detail below in conjunction with the drawings and examples.
如图1所示,一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,其主体部分包括依次连接装配的发生器头部18、发生器上部19和发生器下部25,其中,发生器上部19的内部为主要反应区,可由上方的一次燃烧室10和下方的二次燃烧室11通过喉口组件23连通构成,一次燃烧室10可由耐火组件20环绕而成,耐火组件20材料包括但不限于碳化硅、金属陶瓷、氮化硅等市面上可购买的一种或多种无机金属或非金属材料。发生器下部25可内设喷头13,喷头13上开有若干与水平面成45-80°的斜向下的喷口,发生器下部25底端整体可为收缩喷管结构。As shown in Figure 1, a supercritical hydrothermal combustion steam generator for thermal recovery of heavy oil in an ultra-deep well, its main part includes a generator head 18, a generator upper part 19 and a generator lower part that are sequentially connected and assembled 25, wherein, the interior of the upper part 19 of the generator is the main reaction zone, which can be formed by connecting the upper primary combustion chamber 10 and the lower secondary combustion chamber 11 through the throat assembly 23, and the primary combustion chamber 10 can be formed by surrounding the refractory assembly 20, The material of the refractory component 20 includes, but is not limited to, one or more commercially available inorganic metal or non-metal materials such as silicon carbide, cermet, and silicon nitride. Generator bottom 25 can be provided with sprinkler head 13, has some spouts that become 45-80 ° with the horizontal plane on the shower nozzle 13, and the bottom of generator lower portion 25 can be a contraction nozzle structure as a whole.
发生器头部18为本发明的重要结构,采取端盖形式,其上的核心结构为嘴口5,喷嘴口5中装有纵向贯穿发生器头部18伸入至主要反应区(在分为一次燃烧室10和二次燃烧室11时,则伸入至一次燃烧室10)的喷嘴。其中嘴口5最好能够设置在发生器头部18的中央位置,喷嘴包括喷嘴内胆3、喷嘴外壳4和点火棒1,喷嘴内胆3侧壁开有一次燃料入口2,底端开有若干雾化喷口,点火棒1内插入喷嘴内胆3,喷嘴外壳4上部设有一次氧化剂入口15,喷嘴外壳4下方外部为喷嘴单螺旋结构。二次燃烧室11的下方连接位于发生器下部25的喷头13,其中雾化喷口和喷嘴单螺旋结构均处于主要反应区的上部(在分为一次燃烧室10和二次燃烧室11时,则处于一次燃烧室10的上部)。Generator head 18 is the important structure of the present invention, takes the form of end cap, and the core structure on it is mouth 5, and longitudinal penetration generator head 18 is housed in nozzle mouth 5 and stretches into main reaction zone (in being divided into When primary combustion chamber 10 and secondary combustion chamber 11, then stretch into the nozzle of primary combustion chamber 10). Wherein the mouth 5 preferably can be arranged on the central position of generator head 18, and nozzle comprises nozzle liner 3, nozzle shell 4 and ignition rod 1, and nozzle liner 3 side walls have primary fuel inlet 2, and bottom end has A number of atomizing nozzles, the ignition rod 1 is inserted into the nozzle liner 3, the upper part of the nozzle shell 4 is provided with a primary oxidant inlet 15, and the outside of the nozzle shell 4 is a nozzle single spiral structure. The bottom of the secondary combustion chamber 11 is connected to the spray nozzle 13 located at the lower part 25 of the generator, wherein the atomization nozzle and the single spiral structure of the nozzle are all at the top of the main reaction zone (when divided into the primary combustion chamber 10 and the secondary combustion chamber 11, then in the upper part of the primary combustion chamber 10).
发生器上部19的侧壁可设有二次燃料/氧化剂双通道22,二次燃料/氧化剂双通道22可为双螺旋下降结构,螺旋平面与水平面成10-45°,与此同时发生器头部18上设有与二次燃料/氧化剂双通道22连通的二次燃料入口8和二次氧化剂入口17,二次燃料/氧化剂双通道22下端向内开有若干排倾斜向下的与二次燃烧室11连通的二次燃料/氧化剂混合出孔,该出孔与水平面成45-80°。The side wall of the upper part 19 of the generator can be provided with a secondary fuel/oxidant dual channel 22, and the secondary fuel/oxidant dual channel 22 can be a double spiral descending structure, and the spiral plane is 10-45° from the horizontal plane, while the generator head The part 18 is provided with a secondary fuel inlet 8 and a secondary oxidant inlet 17 communicating with the secondary fuel/oxidant dual channel 22, and the lower end of the secondary fuel/oxidant dual channel 22 is inwardly opened with several rows of obliquely downward and secondary The secondary fuel/oxidant mixing hole communicated with the combustion chamber 11 has an angle of 45-80° to the horizontal plane.
进一步地,发生器上部19的侧壁设有冷却水上通道21,冷却水上通道21位于二次燃料/氧化剂双通道22外侧,发生器头部18上设有与冷却水上通道21连通的冷却水入口9,发生器下部25的上方侧壁设有与冷却水上通道21以竖直孔相连通的冷却水下通道12,冷却水下通道12下方开有连接喷头13的冷却水出口。冷却水上通道21和冷却水下通道12均可为单螺旋下降结构,螺旋平面均与水平面成10-45°。Further, the side wall of the upper part of the generator 19 is provided with a cooling water upper channel 21, the cooling water upper channel 21 is located outside the secondary fuel/oxidant double channel 22, and the generator head 18 is provided with a cooling water inlet communicating with the cooling water upper channel 21 9. The upper side wall of the generator lower part 25 is provided with a cooling water channel 12 connected to the cooling water upper channel 21 through a vertical hole, and a cooling water outlet connected to the nozzle 13 is opened below the cooling water channel 12 . Both the cooling water upper channel 21 and the cooling water lower channel 12 can be of a single spiral descending structure, and the spiral plane is 10-45° from the horizontal plane.
进一步地,本发明还包括了一些实现监测的手段,即,在发生器头部18上设有与一次燃烧室10连通的测压口一7、火焰检测口6和测温口一16,发生器上部19或发生器下部25设置有连通二次燃烧室11的测温口二24,发生器下部25设置有连通喷头13下方区域的测压口二14和测温口三26,从而实现对相应部分的压力与温度的监测。Further, the present invention also includes some monitoring means, that is, the generator head 18 is provided with a pressure measuring port-7, a flame detection port 6 and a temperature measuring port-16 communicating with the primary combustion chamber 10, and The upper part 19 of the generator or the lower part 25 of the generator is provided with a temperature measuring port 2 24 which communicates with the secondary combustion chamber 11, and the lower part 25 of the generator is provided with a pressure measuring port 2 14 and a temperature measuring port 3 26 which are connected to the area below the nozzle 13, so as to realize the Monitoring of pressure and temperature of corresponding parts.
根据以上结构,本发明的工艺流程如下:According to above structure, technological process of the present invention is as follows:
超临界压力下的一定浓度的燃料水溶液经一次燃料入口2进入喷嘴内胆3,经过加热棒1加热后通过底端的雾化喷嘴喷入一次燃烧室10;超临界压力下的氧化剂通过一次氧化剂入口15进入喷嘴外壳4与喷嘴内胆3的环腔内经过下部的螺旋通道起旋进入一次燃烧室10与一次燃料混合点燃并稳定燃烧,反应的高温产物通过喉口组件23,进入二次燃烧室11。The fuel aqueous solution of a certain concentration under supercritical pressure enters the nozzle liner 3 through the primary fuel inlet 2, is sprayed into the primary combustion chamber 10 through the atomizing nozzle at the bottom after being heated by the heating rod 1; the oxidant under supercritical pressure passes through the primary oxidant inlet 15 enters the annular cavity of the nozzle shell 4 and the nozzle liner 3, spins through the lower spiral channel, enters the primary combustion chamber 10, mixes with the primary fuel, ignites and burns stably, and the high-temperature product of the reaction passes through the throat assembly 23 and enters the secondary combustion chamber 11.
另一股超临界压力下的一定浓度的燃料水溶液通过二次燃料入口8进入双螺旋的二次燃料/氧化剂双通道22,另一股超临界压力下的氧化剂通过二次氧化剂入口17进入二次燃料/氧化剂双通道22,两股流体通过经过不同层的螺旋通道流至二次燃料/氧化剂双通道22的下端,两股流体通过二次燃料/氧化剂混合出孔流入二次燃烧室11进行二次燃烧,反应产物通过喷头13上的倾斜向下的喷口喷入发生器下部25内。Another stream of fuel aqueous solution with a certain concentration under supercritical pressure enters the secondary fuel/oxidizer double channel 22 of the double helix through the secondary fuel inlet 8, and another stream of oxidant under supercritical pressure enters the secondary fuel through the secondary oxidizer inlet 17. Fuel/oxidant double channel 22, two streams of fluids flow through the spiral channel through different layers to the lower end of secondary fuel/oxidant dual channel 22, and two streams of fluid flow into secondary combustion chamber 11 through secondary fuel/oxidant mixing outlet hole for secondary combustion Secondary combustion, the reaction product is sprayed into the lower part 25 of the generator through the nozzle 13 inclined downward.
一股超临界压力下的冷却水,通过冷却水入口9进入单螺旋的冷却水上通道21,通过单螺旋往下流,并通过冷却水下通道12开的若干竖直孔流入冷却水下通道的单螺旋通道,随后进入发生器下部25内与反应产物混合,随后混合物通过收缩喷口流出蒸汽发生器。One stream of cooling water under supercritical pressure enters the cooling water upper channel 21 of the single helix through the cooling water inlet 9, flows down through the single helix, and flows into the single channel of the cooling water lower channel through some vertical holes opened in the cooling water channel 12. The spiral channel then enters the lower part 25 of the generator to mix with the reaction product, and then the mixture flows out of the steam generator through the converging nozzle.
综上,本发明公开了一种用于超深井下稠油热采的超临界水热燃烧型蒸汽发生器,包括发生器头部、发生器上部和发生器下部三部分。发生器头部上装有保证超临界水热燃烧反应发生的电加热棒;发生器上部包括一次燃烧室与二次燃烧室以保证燃料与氧化剂的充分超临界水热燃烧反应;发生器下部的喷头与渐缩口保证了反应产物的参数符合油田稠油开采的要求;发生器内的冷却水用于保证发生器不超温以保护发生器安全运行。本装置降低了稠油开采成本,提高热量利用效率,阻止了污染物的排放,实现了深层及海上油藏的高效开采。In summary, the present invention discloses a supercritical hydrothermal combustion steam generator for thermal recovery of heavy oil in an ultra-deep well, including three parts: a generator head, an upper part of the generator and a lower part of the generator. The head of the generator is equipped with an electric heating rod to ensure the occurrence of supercritical hydrothermal combustion reaction; the upper part of the generator includes a primary combustion chamber and a secondary combustion chamber to ensure sufficient supercritical hydrothermal combustion reaction of fuel and oxidant; the nozzle at the lower part of the generator And the tapering port ensures that the parameters of the reaction product meet the requirements of heavy oil production in the oil field; the cooling water in the generator is used to ensure that the generator does not overheat to protect the safe operation of the generator. The device reduces the cost of heavy oil exploitation, improves heat utilization efficiency, prevents the discharge of pollutants, and realizes efficient exploitation of deep and offshore oil reservoirs.
以上,仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above is only a specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in this document. within the scope of protection of the invention.
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5571423A (en) * | 1994-10-14 | 1996-11-05 | Foster Wheeler Development Corporation | Process and apparatus for supercritical water oxidation |
CN101067372A (en) * | 2007-06-07 | 2007-11-07 | 苏州新阳光机械制造有限公司 | High-pressure mixed gas generating device for gas injection machine in petroleum thermal recovery |
CN102353033A (en) * | 2011-08-09 | 2012-02-15 | 江苏大江石油科技有限公司 | High-temperature high-pressure combustion system for supercritical compound heat carrier generator |
CN103776038A (en) * | 2014-01-25 | 2014-05-07 | 西安市万丰能源环保科技有限公司 | Multifunctional supercritical water thermal combustion device |
CN106630287A (en) * | 2016-12-30 | 2017-05-10 | 西安理工大学 | Supercritical hydrothermal combustion treatment and steam injection system for oil extraction waste liquid |
CN108837792A (en) * | 2018-08-14 | 2018-11-20 | 成都九翼环保科技有限公司 | A kind of complete waterpower mixed type overcritical water oxidization reactor and its application in sewage recycling utilization |
CN109237508A (en) * | 2018-08-14 | 2019-01-18 | 成都九翼环保科技有限公司 | A kind of Liqiud-gas mixing device and its application for overcritical hydro-thermal combustion reactor |
CN210772088U (en) * | 2019-10-22 | 2020-06-16 | 西安交通大学 | A supercritical hydrothermal combustion type steam generator for ultra-deep downhole heavy oil thermal recovery |
-
2019
- 2019-10-22 CN CN201911007846.7A patent/CN110617466B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5571423A (en) * | 1994-10-14 | 1996-11-05 | Foster Wheeler Development Corporation | Process and apparatus for supercritical water oxidation |
CN101067372A (en) * | 2007-06-07 | 2007-11-07 | 苏州新阳光机械制造有限公司 | High-pressure mixed gas generating device for gas injection machine in petroleum thermal recovery |
CN102353033A (en) * | 2011-08-09 | 2012-02-15 | 江苏大江石油科技有限公司 | High-temperature high-pressure combustion system for supercritical compound heat carrier generator |
CN103776038A (en) * | 2014-01-25 | 2014-05-07 | 西安市万丰能源环保科技有限公司 | Multifunctional supercritical water thermal combustion device |
CN106630287A (en) * | 2016-12-30 | 2017-05-10 | 西安理工大学 | Supercritical hydrothermal combustion treatment and steam injection system for oil extraction waste liquid |
CN108837792A (en) * | 2018-08-14 | 2018-11-20 | 成都九翼环保科技有限公司 | A kind of complete waterpower mixed type overcritical water oxidization reactor and its application in sewage recycling utilization |
CN109237508A (en) * | 2018-08-14 | 2019-01-18 | 成都九翼环保科技有限公司 | A kind of Liqiud-gas mixing device and its application for overcritical hydro-thermal combustion reactor |
CN210772088U (en) * | 2019-10-22 | 2020-06-16 | 西安交通大学 | A supercritical hydrothermal combustion type steam generator for ultra-deep downhole heavy oil thermal recovery |
Cited By (17)
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---|---|---|---|---|
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CN112811567B (en) * | 2021-01-20 | 2022-06-03 | 贵州航天朝阳科技有限责任公司 | Supercritical water oxidation reaction device and control method |
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US12098845B2 (en) * | 2021-08-31 | 2024-09-24 | Xi'an Jiaotong University | Supercritical hydrothermal combustion device |
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