石油与天然气化工
石油與天然氣化工
석유여천연기화공
CHEMICAL ENGINEERING OF OIL AND GAS
2009年
6期
465-468
,共4页
周厚安%唐永帆%王川%王东海
週厚安%唐永帆%王川%王東海
주후안%당영범%왕천%왕동해
硫化氢%酸性天然气%气体水合物%动力学抑制剂%性能评价
硫化氫%痠性天然氣%氣體水閤物%動力學抑製劑%性能評價
류화경%산성천연기%기체수합물%동역학억제제%성능평개
hydrogen sulfide%sour natural gas%gas hydrate%hydrate kinetic inhibitor%performance evaluation
随着近年来国内外大量高含硫酸性气田的不断开发,天然气水合物的形成与堵塞防治问题引起了科研生产工作者的极大关注.甲醇、乙二醇等传统热力学抑制剂有毒、药剂用量大,会产生大量酸性污水难于处理,不能完全满足防止高含硫酸性天然气水合物形成的需要.本文介绍了新型动力学水合物抑制剂GHI-1的制备、性能评价方法及对含硫酸性天然气水合物形成抑制的性能评价结果.评价结果表明,动力学抑制剂GHI-1对于防止高含硫化氢酸性气体的甲烷天然气Ⅰ型结构水合物的形成具有较好的抑制效果.对于H_2S含量为0.82%、CO_2含量为2.43%的低含硫甲烷天然气,在8.0 MPa、5℃(过冷度为8.2℃)的条件下,加注5%的动力学抑制剂GHI-1,可使水合物形成时间延长至3 h以上,其药剂加量相当于乙二醇加量的1/4.对于H_2S含量为7.92%、CO_2含量为1.61%的高含硫甲烷天然气,在8.0 MPa、10℃(过冷度为9.85℃)的条件下,加注10%的动力学抑制剂GHI-1,可使水合物形成时间延长至3 h以上,其药剂加量相当于甲醇加量的1/2和乙二醇加量的1/3.
隨著近年來國內外大量高含硫痠性氣田的不斷開髮,天然氣水閤物的形成與堵塞防治問題引起瞭科研生產工作者的極大關註.甲醇、乙二醇等傳統熱力學抑製劑有毒、藥劑用量大,會產生大量痠性汙水難于處理,不能完全滿足防止高含硫痠性天然氣水閤物形成的需要.本文介紹瞭新型動力學水閤物抑製劑GHI-1的製備、性能評價方法及對含硫痠性天然氣水閤物形成抑製的性能評價結果.評價結果錶明,動力學抑製劑GHI-1對于防止高含硫化氫痠性氣體的甲烷天然氣Ⅰ型結構水閤物的形成具有較好的抑製效果.對于H_2S含量為0.82%、CO_2含量為2.43%的低含硫甲烷天然氣,在8.0 MPa、5℃(過冷度為8.2℃)的條件下,加註5%的動力學抑製劑GHI-1,可使水閤物形成時間延長至3 h以上,其藥劑加量相噹于乙二醇加量的1/4.對于H_2S含量為7.92%、CO_2含量為1.61%的高含硫甲烷天然氣,在8.0 MPa、10℃(過冷度為9.85℃)的條件下,加註10%的動力學抑製劑GHI-1,可使水閤物形成時間延長至3 h以上,其藥劑加量相噹于甲醇加量的1/2和乙二醇加量的1/3.
수착근년래국내외대량고함류산성기전적불단개발,천연기수합물적형성여도새방치문제인기료과연생산공작자적겁대관주.갑순、을이순등전통열역학억제제유독、약제용량대,회산생대량산성오수난우처리,불능완전만족방지고함류산성천연기수합물형성적수요.본문개소료신형동역학수합물억제제GHI-1적제비、성능평개방법급대함류산성천연기수합물형성억제적성능평개결과.평개결과표명,동역학억제제GHI-1대우방지고함류화경산성기체적갑완천연기Ⅰ형결구수합물적형성구유교호적억제효과.대우H_2S함량위0.82%、CO_2함량위2.43%적저함류갑완천연기,재8.0 MPa、5℃(과랭도위8.2℃)적조건하,가주5%적동역학억제제GHI-1,가사수합물형성시간연장지3 h이상,기약제가량상당우을이순가량적1/4.대우H_2S함량위7.92%、CO_2함량위1.61%적고함류갑완천연기,재8.0 MPa、10℃(과랭도위9.85℃)적조건하,가주10%적동역학억제제GHI-1,가사수합물형성시간연장지3 h이상,기약제가량상당우갑순가량적1/2화을이순가량적1/3.
With a large number of developing sour natural gas fields at home and abroad in recent years, many researchers take extra attention to prevent hydrate plugging problems. The traditional thermodynamic inhibitors have been used to prevent hydrate forming during oil & gas production and gathering and transportation, such as methanol and ethylene glycol, etc. but this kind of inhibitors has some disadvantages, which can not meet the needs of production and operation in sour natural gas fields. The preparation process and performance evaluation results of the new hydrate kinetic inhibitors GHI-1 were introduced in this paper. The evaluation test results showed that hydrate kinetic inhibitors GHI - 1 can effectively prevent the forming of methane hydrates of structure I in the natural gas with high H_2S contents. For the natural gas containing 0. 82% H_2S and 2.43% CO_2, 5% GHI-1 inhibitors can delay the hydrate formation time to exceed 3 hours at 8. 0 MPa,5℃ (sub-cooling:8. 2℃), corresponding with 1/4 dosages of ethylene glycol at the same conditions. For natural gas containing7.92% H_2S and 1.61% CO_2, 10% GHI-1 inhibitors can delay hydrate formation time to exceed 3 hours at the 8. 0 MPa, 10℃ (subcooling: 9. 85℃), corresponding with 1/2 dosages of methanol or 1/3 dosages of ethylene glycol at the same conditions.