某逆流吸收塔塔底排出液中含溶质摩尔分数[tex=4.571x1.357]hnsjkp7yQB1hY+4HBL6Hm8KTS9ZzzzccyfsRoUNvrow=[/tex], 进口气体中含溶质体积分数为[tex=2.143x1.143]3my6+SrcyYc3Tkde7CdllA==[/tex]。操作压力为[tex=3.214x1.0]bCvJNAQZrIE9CYj4Z/VZTuOilkVGNc/EO/IaqaljjIc=[/tex], 气液平衡关系为[tex=2.857x1.214]APPXuyIGjl9TuV0AHwGnkH/B8jTa1krE5AvnlDTq9jY=[/tex]。现将操作压力由[tex=3.214x1.0]bCvJNAQZrIE9CYj4Z/VZTuOilkVGNc/EO/IaqaljjIc=[/tex]增至[tex=3.214x1.0]J2MdVFikAwWMUWrx0aYut4c9Xnb1ihuEXLqke/A/hWE=[/tex], 问塔底推动力[tex=2.929x1.357]c8PeckMEmQiu3+ZwF5y566IBla7DA6SAHAEv0PamfMosurfN3JlZqGxLpRrBMIusoBm9XzF+eAZ9fPfCbgTUhA==[/tex]及[tex=2.929x1.357]foZQl5OKDxiJt9ftYEdz7jszQvoYKJYhGAdGAnmL7y+IreTzxydAk9Ur2JTsenkVKRLRUleW+MzyfGGvb3LQbw==[/tex]各增加至原有的多少倍。