1) huff-and-puff steam injection
蒸汽吞吐法
2) cyclic steam stimulation
蒸汽吞吐
1.
Calculating models for heating radius of cyclic steam stimulation and formation parameters in horizontal well after soaking;
水平井蒸汽吞吐加热半径和地层参数计算模型
2.
Steam injection design by method of climax descent for cyclic steam stimulation;
蒸汽吞吐极点降维法注汽量设计
3.
Adjustment technology for the middle-last stage of cyclic steam stimulation on Ng5 thin sand heavy oil loop in Zhong2zhong block, Gudao Oilfield;
孤岛油田中二中Ng5薄层稠油环蒸汽吞吐中后期调整技术
3) huff and puff
蒸汽吞吐
1.
The dynamic characteristic of producing wells during the huff and puff in the Xinzhuang field,Henan,China;
新庄特稠油藏蒸汽吞吐井动态特征及水侵识别分析
2.
Analysis of the efficiency of huff and puff in the reservoir of edge water invasion and fault block;
边水断块油藏蒸汽吞吐开发效果分析
3.
Development and application of sand control agent of high temperature foam resin for wells of huff and puff;
稠油蒸汽吞吐井高温泡沫树脂防砂剂的研制与应用
4) steam soaking
蒸汽吞吐
1.
Numerical simulation study for parameter optimization of steam soaking,Xinglongtai reservoir, Du 32 block.;
杜32断块区兴隆台油层蒸汽吞吐参数优化数值模拟研究
2.
Determine optimal well shut-in time for steam soaking by applying Producing test.;
应用试井方法确定蒸汽吞吐最佳焖井时间
3.
Study on features of remaining oil during steam soaking in shallow heavy oil reservoir of Xinjiang;
新疆浅层稠油油藏蒸汽吞吐阶段剩余油特征研究
5) steam soak
蒸汽吞吐
1.
Study on the thermal cracking of heavy oil during steam soak;
稠油蒸汽吞吐热裂解行为研究
2.
Study on cyclic carbon dioxide injection after steam soak in heavy oil reservoir;
稠油油藏蒸汽吞吐后转注CO_2吞吐开采研究
3.
Study on water existing state of steam soak in Gaosheng oil field;
高升油田蒸汽吞吐存水状况研究
6) steam stimulation
蒸汽吞吐
1.
Optimization design of profile control parameters for steam stimulation wells;
蒸汽吞吐汽窜调剖参数优化设计研究
2.
Study on relationship between bottom water and interbed of heavy oil during steam stimulation.;
底水稠油油藏蒸汽吞吐底水与夹层关系数值模拟
3.
Remaining oil distribution in shallow, thin and super-heavy oil reservoir of Henan Oilfield after steam stimulation;
浅薄层特、超稠油注蒸汽吞吐后剩余油分布研究
补充资料：低能耗蒸汽转化法
分子式：
CAS号：
性质：对传统的天然气蒸汽转化传统方法的革新以达到了增产节能的效果。主要革新：(1)一段转化炉采用换热式，出二段转化炉的高温气体不用于产生高压蒸汽，用作一段转化炉所需热量的加热介质；(2)一段转化炉采用较温和的转化温度，二段转化炉加入过量空气，工艺气中过量的氮采用深冷或变压吸附法除去；(3)降低一段转化炉的H2O/C，由3.5降至2.7左右，需要采用适当低H2O/C的转化催化剂。
CAS号：
性质：对传统的天然气蒸汽转化传统方法的革新以达到了增产节能的效果。主要革新：(1)一段转化炉采用换热式，出二段转化炉的高温气体不用于产生高压蒸汽，用作一段转化炉所需热量的加热介质；(2)一段转化炉采用较温和的转化温度，二段转化炉加入过量空气，工艺气中过量的氮采用深冷或变压吸附法除去；(3)降低一段转化炉的H2O/C，由3.5降至2.7左右，需要采用适当低H2O/C的转化催化剂。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条