Center for Hydrate Research, Chemical & Biological Engineering Department, Colorado School of Mines , Golden, Colorado 80401, United States.
Langmuir. 2017 Oct 24;33(42):11299-11309. doi: 10.1021/acs.langmuir.7b02676. Epub 2017 Oct 3.
The interfacial properties and mechanisms of gas hydrate systems play a major role in controlling their interparticle and surface interactions, which is desirable for nearly all energy applications of clathrate hydrates. In particular, preventing gas hydrate interparticle agglomeration and/or particle-surface deposition is critical to the prevention of gas hydrate blockages during the exploration and transportation of oil and gas subsea flow lines. These agglomeration and deposition processes are dominated by particle-particle cohesive forces and particle-surface adhesive force. In this study, we present the first direct measurements on the cohesive and adhesive forces studies of the CH/CH gas hydrate in a liquid hydrocarbon-dominated system utilizing a high-pressure micromechanical force (HP-MMF) apparatus. A CH/CH gas mixture was used as the gas hydrate former in the model liquid hydrocarbon phase. For the cohesive force baseline test, it was found that the addition of liquid hydrocarbon changed the interfacial tension and contact angle of water in the liquid hydrocarbon compared to water in the gas phase, resulting in a force of 23.5 ± 2.5 mN m at 3.45 MPa and 274 K for a 2 h annealing time period in which hydrate shell growth occurs. It was observed that the cohesive force was inversely proportional to the annealing time, whereas the force increased with increasing contact time. For a longer contact time (>12 h), the force could not be measured because the two hydrate particles adhered permanently to form one large particle. The particle-surface adhesive force in the model liquid hydrocarbon was measured to be 5.3 ± 1.1 mN m under the same experimental condition. Finally, with a 1 h contact time, the hydrate particle and the carbon steel (CS) surface were sintered together and the force was higher than what could be measured by the current apparatus. A possible mechanism is presented in this article to describe the effect of contact time on the particle-particle cohesive force based on the capillary liquid bridge model. A model adapted from the capillary liquid bridge equation has been used to predict the particle-particle cohesive force as a function of contact time, showing close agreement with the experimental data. By comparing the cohesive forces results from gas hydrates for both gas and liquid bulk phases, the surface free energy of a hydrate particle was calculated and found to dominate the changes in the interaction forces with different continuous bulk phases.
天然气水合物体系的界面特性和机理在控制其颗粒间和表面相互作用方面起着重要作用,这对于天然气水合物的几乎所有能源应用都是理想的。特别是,防止天然气水合物颗粒间团聚和/或颗粒-表面沉积对于防止海底油气输送管道中天然气水合物堵塞至关重要。这些团聚和沉积过程主要由颗粒间的内聚力和颗粒-表面的粘附力控制。在这项研究中,我们首次利用高压微机械力(HP-MMF)装置直接测量了在以液态烃为主的体系中 CH/CH 天然气水合物的内聚和粘附力。在模型液态烃相中,使用 CH/CH 天然气混合物作为天然气水合物形成物。对于内聚力基线测试,发现与气相中的水相比,液态烃的加入改变了液态烃中的水的界面张力和接触角,导致在 3.45 MPa 和 274 K 下,在 2 h 的退火时间内,水合壳生长过程中,力为 23.5 ± 2.5 mN m。观察到内聚力与退火时间成反比,而力随接触时间的增加而增加。对于较长的接触时间(>12 h),由于两个水合颗粒永久粘附形成一个大颗粒,因此无法测量力。在相同的实验条件下,模型液态烃中的颗粒-表面粘附力测量值为 5.3 ± 1.1 mN m。最后,在 1 h 的接触时间内,水合颗粒和碳钢(CS)表面烧结在一起,力高于当前仪器所能测量的力。本文提出了一种可能的机制,根据毛细液桥模型描述接触时间对颗粒间内聚力的影响。使用从毛细液桥方程改编而来的模型来预测颗粒间内聚力作为接触时间的函数,与实验数据吻合较好。通过比较气相和液相两种连续相的天然气水合物的内聚力结果,计算出水合颗粒的表面自由能,发现其对不同连续相下相互作用力的变化起主导作用。