Based on the above mentioned research results, Well PD1HF in the Laochangping anticline was selected for adsorbed gas desorption process research. This well, with the target layer at 979 m (VD) and the horizontal section of 1510 m long, revealed the initial daily gas production rate of 1.1×10
4 m
3 during test under the casing pressure of 0.35 MPa. The production test is divided into three stages, including jet pump production, hydraulic rodless pump production, and flow production. In the stage of jet pump production, the daily liquid production was less than 5 m
3, the bottomhole flow pressure declined from 4.72 MPa to about 3.9 MPa, the daily casing pressure drop was 0.001 MPa, and the equivalent dynamic liquid level depth was 585 m. Due to high liquid level, low daily liquid production and serious liquid loading at the bottomhole, the formation pressure in the reservoir stimulation zone could hardly decrease to the sensitive desorption pressure, and the gas well productivity could not be liberated sufficiently. As a result, it showed the characteristics of low gas production rate, casing pressure and liquid production rate, and long low-pressure stable production period with casing pressure of 0.4 MPa and daily gas production of (0.6-0.8)×10
4 m
3.
[21]. According to the desorption laws of adsorbed gas, the adsorbed gas cannot be desorbed and produced in a great quantity unless the formation pressure is lower than the sensitive desorption pressure. Therefore, the production process was optimized, and the hydraulic rodless pump was selected for drainage enhancement to decrease the flow pressure. The daily liquid production was increased to 12.0-38.5 m
3. After 21 d of liquid drainage, the bottomhole flow pressure dropped to 1.95 MPa, the equivalent dynamic liquid level declined to about 810 m, the flow regime in the wellbore transited gradually from pure liquid-bubble flow (fluid density of 949 kg/m
3) to slug flow-annulus flow (fluid density decreasing from 900 kg/m
3 to 200 kg/m
3), and the production rate increased to 4.4×10
4 m
3/d with interim cumulative gas production of 13×10
4 m
3. At present, it is in the stage of flow production, when the bottomhole flow pressure drops from 1.95 MPa to 1.39 MPa, and the formation pressure in the reservoir stimulation zone decreases below the sensitive desorption pressure. In this situation, adsorbed gas begins to desorb greatly and transforms into the regime of mist flow (fluid density less than 200 kg/m
3), so that the stable production of flow carrying fluid is realized with daily gas production of (4.4-4.6)×10
4 m
3, daily liquid production of 4.7 m
3, and the production rate and the casing pressure are stable. The EUR evaluated according to the flowing material balance based on the latest production data is 0.36×10
8 m
3, which means the effective production of shallow normal-pressure adsorbed gas.