CN113000029B - 一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 - Google Patents
一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 Download PDFInfo
- Publication number
- CN113000029B CN113000029B CN202110227850.5A CN202110227850A CN113000029B CN 113000029 B CN113000029 B CN 113000029B CN 202110227850 A CN202110227850 A CN 202110227850A CN 113000029 B CN113000029 B CN 113000029B
- Authority
- CN
- China
- Prior art keywords
- suspension
- straw
- oil
- preparation
- bio
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/08—Polysaccharides
- B01D71/10—Cellulose; Modified cellulose
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/12—Naturally occurring clays or bleaching earth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
- B01J20/28038—Membranes or mats made from fibers or filaments
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4806—Sorbents characterised by the starting material used for their preparation the starting material being of inorganic character
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Inorganic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本发明公开一种基于农业秸秆纤维的高性能脱汞疏油过滤纤维膜及其制备方法,本发明利用价廉、易得的天然植物纤维(秸秆)为原料,通过简单的水热预处理、强化汞离子靶向吸附、有机无机复合纤维强化和疏油改性系列方法,制备得到的适用于油气田污水中含有的汞离子吸附以及汞悬浮物(包含单质汞)过滤去除的生物基纤维膜,同时对油及有机聚合物等与水具有良好的分离性能。
Description
技术领域
本发明涉及秸秆纤维吸附过滤膜的制备领域技术领域,尤其涉及适用于油气田领域同时具有除汞、疏油以及悬浮物过滤性能的复合纤维膜的制备方法。
背景技术
随着高含汞油气田的生产和开发,天然气等经过脱汞处理后汞富集在油气田污水中,含汞油气田污水成分复杂,含有悬浮物、油、汞等,含汞油气田水可能破坏生态环境、影响正常生产和危害操作人员健康。我国油气田含汞污水排放须遵循GB8978—1996《污水综合排放标准》、陆上石油天然气开采工业污染物排放标准以及Q/SY TZ 0086-2017等的规定:含汞油气田排放水中不得检出烷基汞,总汞含量不高于0.05mg/L,含油量不高于5mg/L,悬浮固体含量不高于2mg/L。然而在油气田污水环境中汞、油以及聚合物并不是单一存在的,而是相互影响,相互作用,从而影响汞在环境中的赋存形态。例如在该环境中汞易和有机物形成络合物,或油中包汞等状态。目前针对油气田污水中汞去除的现有技术中最广泛使用的汞处理方法是化学沉淀-絮凝法,该方法需要投放大量重金属捕捉剂,产生大量含汞含油危废,并且由于油和聚合物的存在导致直接捕捉汞离子的效率低。与化学沉淀-絮凝法相比,吸附法具有高效性,被视为最有实用价值和推广潜力的技术,但目前几乎所有研究资料与专利产品所研发的吸附剂都需要对污水进行高级氧化、电化学以及膜过滤等各种预处理,尤其是在油气田领域,对吸附剂段进水水质要求苛刻,同时价格过高导致实际应用困难。所以强化汞离子靶向吸附、以及疏油改性等制备得到的适用于油气田污水中含有的汞离子吸附以及汞悬浮物(包含单质汞)过滤去除的材料具有十分重要的意义。同时我国作为一个农业大国,每年都会产生大量的废弃农业秸秆,他们具有易得、量大、可生物降解、环境友好等特点,对秸秆资源化利用开辟了一条合理利用的新途径,具有极大的社会效益和生态效益。本发明主要针对油气田含汞污水的处理,只需一步即可去除废水中的乳化油、有机聚合物、汞离子、汞悬浮物(包含单质汞)以及悬浮固体。
发明内容
为解决上述的缺点和不足,本发明的目的在于提供一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,解决了油气田污水中复杂恶劣工况下对汞去除效果差、处理不达标的问题。
具体技术方案如下:
一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,包括以下步骤:
1)将秸秆原料放入蒸煮罐内,加入自来水蒸煮,然后粉碎、筛分后得到秸秆纤维悬浮液;
2)将筛分后的秸秆纤维悬浮液用碱液进行碱洗1h~24h去除杂质,将秸秆纤维悬浮液通过抽滤装置滤出,再用水清洗,直至滤液呈中性;
3)碱洗、抽滤、水洗后的秸秆纤维用乙醇配置5wt%~25wt%的制膜悬浮液,然后向其添加多胺螯合剂和聚乙烯醇进行胺化反应处理,并将混合物搅拌均匀化10min~60min;
4)将海泡石纤维添加进混合物中机械搅拌1min~60min以获得均匀悬浮液;
5)然后向均匀悬浮液中添加两性氟表面活性剂,并在室温下将该混合物磁力搅拌10min~60min;
6)将正硅酸乙酯添加到悬浮液中,然后进行磁力搅拌直到正硅酸乙酯完全水解;
7)滴加硅烷偶联剂,在常温下连续搅拌1h~24h,得到产品悬浮液;
8)抽滤并用水洗涤至中性,鼓暖风风干制备得到生物基吸附过滤纤维膜。
优选为,所述步骤1)中,秸秆与自来水的固液比1:5~1:10;蒸煮温度在150℃~200℃,时间为10min~60min。
优选为,所述步骤1)中,粉碎、筛分后秸秆纤维悬浮液中秸秆长度在0.5mm~1.5mm,宽度在20μm~40μm。
优选为,步骤1)中秸秆原料为玉米秸秆、稻草秸秆、小麦秸秆、棉花秸秆、辣椒秸秆中任意一种或任意几种混合。
优选为,所述步骤2)中碱液为氢氧化钠、氢氧化钾以及氨水中任意一种或任意几种混合;浓度为0.5mol/L~10mol/L。
优选为,所述步骤3)中多胺螯合剂为四甲基乙二胺、二乙烯三胺、三乙烯四胺、四乙烯五胺中任意一种或任意几种混合,占制膜悬浮液总量1wt%~10wt%;聚乙烯醇占制膜悬浮液总量0.1wt%~10wt%。
优选为,所述步骤4)中海泡石纤维占制膜悬浮液总量0.05wt%~5wt%。
优选为,所述步骤5)中两性氟表面活性剂为杜邦Capstone FS-50两性氟表面活性剂;占制膜悬浮液总量0.1wt%~10wt%。
优选为,所述步骤6)中正硅酸乙酯占制膜悬浮液总量0.1wt%~10wt%。
优选为,所述步骤7)中硅烷偶联剂占制膜悬浮液总量0.1wt%~10wt%。
本发明的有益效果:
以廉价、量大、易得、孔道结构丰富、吸附性能良好且易改性的天然农业秸秆纤维为原料,根据本发明方法制备得到的秸秆纤维疏油吸汞材料不仅成本低、可生物降解性,同时可一步去除废水中的乳化油、有机聚合物、汞离子、汞悬浮物(包含单质汞)以及悬浮固体。
另外海泡石纤维的添加不但可以增加纤维膜强度,其在矿物中的高吸附性能也可增强对汞元素的吸附。而聚乙烯醇粘结剂的加入克服了海泡石纤维缺乏羟基及氨基的缺点,增加了与秸秆纤维的结合力,发挥了无机有机纤维各自的优势。
同时利用两性氟表面活性剂等改性方法对秸秆纤维进行亲水疏油改性,操作简单、成本低,还可实现亲水疏油吸汞性能,在油气田污水中汞去除回收治理方面具有显著的竞争优势。
具体实施方式:
实施例1
将棉花秸秆原料放入蒸煮罐内,按照固液比1:5往罐内加入自来水在150℃温度下蒸煮45min,然后粉碎、筛分后得到长度在0.9mm,宽度在25μm的棉花秸秆纤维悬浮液。
将筛分后的棉花秸秆纤维悬浮液用0.5mol/L的氢氧化钠进行碱洗12h去除杂质,将棉花秸秆纤维悬浮液通过抽滤装置滤出,再用水清洗,直至滤液呈中性。
碱洗抽滤水洗后的棉花秸秆纤维用乙醇配置20wt%的制膜悬浮液,然后向其添加占制膜悬浮液总量5wt%的四甲基乙二胺螯合剂和1wt%的聚乙烯醇进行胺化反应处理,并将混合物搅拌均匀化45min。
将占制膜悬浮液总量0.1wt%的海泡石纤维添加进混合物中机械搅拌45min以获得均匀悬浮液;
然后向悬浮液中添加占制膜悬浮液总量3wt%杜邦Capstone FS-50两性氟表面活性剂,并在室温下将该混合物磁力搅拌45min;
将占制膜悬浮液总量3wt%正硅酸乙酯添加到悬浮液中,然后进行磁力搅拌直到正硅酸乙酯完全水解;
滴加占制膜悬浮液总量1wt%的硅烷偶联剂,在常温下连续搅拌12h,得到产品悬浮液;
抽滤并用水洗涤至中性,鼓暖风风干制备得到棉花秸秆基吸附过滤纤维膜。
制得棉花秸秆基吸附过滤纤维膜对新疆区域某含汞气田水进行处理,结果如下表:
实施例2
将稻草秸秆原料放入蒸煮罐内,按照固液比1:10往罐内加入自来水在200℃温度下蒸煮60min,然后粉碎、筛分后得到长度在1mm,宽度在30μm的稻草秸秆纤维悬浮液;
将筛分后的稻草秸秆纤维悬浮液用5mol/L的氢氧化钾进行碱洗1h去除杂质,将稻草秸秆纤维悬浮液通过抽滤装置滤出,再用水清洗,直至滤液呈中性;
碱洗抽滤水洗后的稻草秸秆纤维用乙醇配置25wt%的制膜悬浮液,然后向其添加占制膜悬浮液总量1wt%的二乙烯三胺的多胺螯合剂和0.1wt%的聚乙烯醇进行胺化反应处理,并将混合物搅拌均匀化30min;
将占制膜悬浮液总量0.05wt%的海泡石纤维添加进混合物中机械搅拌30min以获得均匀悬浮液;
然后向悬浮液中添加占制膜悬浮液总量0.1wt%杜邦Capstone FS-50两性氟表面活性剂,并在室温下将该混合物磁力搅拌30min;将占制膜悬浮液总量0.1wt%正硅酸乙酯添加到悬浮液中,然后进行磁力搅拌直到正硅酸乙酯完全水解;
滴加占制膜悬浮液总量3wt%的硅烷偶联剂,在常温下连续搅拌1h,得到产品悬浮液;
抽滤并用水洗涤至中性,鼓暖风风干制备得到稻草秸秆基吸附过滤纤维膜。
制得的稻草秸秆基吸附过滤纤维膜对新疆区域某含汞气田水进行处理,结果如下表:
实施例3
将玉米秸秆原料放入蒸煮罐内,按照固液比1:8往罐内加入自来水在180℃温度下蒸煮60min,然后粉碎、筛分后得到长度在1.5mm,宽度在40μm的玉米秸秆纤维悬浮液;
将筛分后的秸秆纤维悬浮液用10mol/L的氨水进行碱洗24h去除杂质,将玉米秸秆纤维悬浮液通过抽滤装置滤出,再用水清洗,直至滤液呈中性;
碱洗抽滤水洗后的秸秆纤维用乙醇配置10wt%的制膜悬浮液,然后向其添加占制膜悬浮液总量1wt%的四乙烯五胺的多胺螯合剂和5wt%的聚乙烯醇进行胺化反应处理,并将混合物搅拌均匀化60min;
将占制膜悬浮液总量5wt%的海泡石纤维添加进混合物中机械搅拌60min以获得均匀悬浮液;
然后向悬浮液中添加占制膜悬浮液总量5wt%的杜邦Capstone FS-50两性氟表面活性剂,并在室温下将该混合物磁力搅拌60min;
将占制膜悬浮液总量5wt%正硅酸乙酯添加到悬浮液中,然后进行磁力搅拌直到正硅酸乙酯完全水解;
滴加占制膜悬浮液总量5wt%的硅烷偶联剂,在常温下连续搅拌24h,得到产品悬浮液;
抽滤并用水洗涤至中性,鼓暖风风干制备得到玉米秸秆基吸附过滤纤维膜。
制得的玉米秸秆基吸附过滤纤维膜对东北区域某含汞油气田水进行处理,结果如下表:
以上所述,并非对本发明作任何形式上的限制,任何未脱离本发明技术方案内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。
Claims (10)
1.一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,包括以下步骤:
1)将秸秆原料放入蒸煮罐内,加入自来水蒸煮,然后粉碎、筛分后得到秸秆纤维悬浮液;
2)将筛分后的秸秆纤维悬浮液用碱液进行碱洗去除杂质,将秸秆纤维悬浮液通过抽滤,再用水清洗,直至滤液呈中性;
3)碱洗、抽滤、水洗后的秸秆纤维用乙醇配置5wt%~25wt%的制膜悬浮液,然后向其添加多胺螯合剂和聚乙烯醇进行胺化反应处理,并将混合物搅拌均匀化;
4)将海泡石纤维添加进混合物中搅拌以获得均匀悬浮液;
5)然后向均匀悬浮液中添加两性氟表面活性剂,并在室温下将该混合物搅拌10min~60min;
6)将正硅酸乙酯添加到悬浮液中,然后进行搅拌直到正硅酸乙酯完全水解;
7)滴加硅烷偶联剂,在常温下连续搅拌1h~24h,得到产品悬浮液;
8)抽滤并用水洗涤至中性,鼓暖风风干制备得到生物基吸附过滤纤维膜。
2.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤1)中,秸秆与自来水的固液比1:5~1:10;蒸煮温度在150℃~200℃,时间为10 min~60min。
3.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤1)中,粉碎、筛分后秸秆纤维悬浮液中秸秆长度在0.5mm~1.5mm,宽度在20μm~40μm。
4.根据权利要求1所述的适用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,步骤1)中秸秆原料为玉米秸秆、稻草秸秆、小麦秸秆、棉花秸秆、辣椒秸秆中任意一种或任意几种混合。
5.根据权利要求1所述的适用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤2)中碱液为氢氧化钠、氢氧化钾以及氨水中任意一种或任意几种混合;浓度为0.5mol/L~10mol/L。
6.根据权利要求1所述的适用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤3)中多胺螯合剂为四甲基乙二胺、二乙烯三胺、三乙烯四胺、四乙烯五胺中任意一种或任意几种混合,占制膜悬浮液总量1wt%~10wt%;聚乙烯醇占制膜悬浮液总量0.1wt%~10wt%。
7.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤4)中海泡石纤维占制膜悬浮液总量0.05wt%~5wt%。
8.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤5)中两性氟表面活性剂为杜邦Capstone FS-50两性氟表面活性剂;占制膜悬浮液总量0.1wt%~10wt%。
9.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤6)中正硅酸乙酯占制膜悬浮液总量0.1wt%~10wt%。
10.根据权利要求1所述的一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法,其特征在于,所述步骤7)中硅烷偶联剂占制膜悬浮液总量0.1wt%~10wt%。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110227850.5A CN113000029B (zh) | 2021-03-01 | 2021-03-01 | 一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110227850.5A CN113000029B (zh) | 2021-03-01 | 2021-03-01 | 一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113000029A CN113000029A (zh) | 2021-06-22 |
CN113000029B true CN113000029B (zh) | 2022-11-25 |
Family
ID=76402002
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110227850.5A Active CN113000029B (zh) | 2021-03-01 | 2021-03-01 | 一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113000029B (zh) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113750823B (zh) * | 2021-07-19 | 2022-11-25 | 青岛科技大学 | 一种天然生物质材料油水分离膜及其制备方法和用途 |
CN113600147B (zh) * | 2021-08-10 | 2023-07-14 | 贵州师范大学 | 一种重金属离子吸附纤维膜材料的制备方法 |
CN115364820A (zh) * | 2022-08-21 | 2022-11-22 | 贵州师范大学 | 一种疏油性液相汞离子吸附材料的制备方法 |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6383388B1 (en) * | 1995-08-08 | 2002-05-07 | The Regents Of The University Of California | Water treatment process and system for metals removal using Saccharomyces cerevisiae |
CN103357277A (zh) * | 2013-07-24 | 2013-10-23 | 浙江师范大学 | 一种具有重金属离子吸附功能的超滤膜及其制备方法 |
WO2016125041A1 (en) * | 2015-02-03 | 2016-08-11 | Nawani Neelu | A method for removal of metals from aqueous solutions using bio adsorbents |
CN106215845A (zh) * | 2016-08-26 | 2016-12-14 | 中国石油天然气股份有限公司 | 一种铜基脱汞吸附剂的脱汞及再生方法 |
CN106237985A (zh) * | 2016-08-16 | 2016-12-21 | 四川师范大学 | 一种秸秆基选择性除汞材料及其制备方法和应用 |
CN106914222A (zh) * | 2015-12-28 | 2017-07-04 | 沈阳中科环境工程科技开发有限公司 | 一种用于去除液相汞的吸附剂及其制备方法和使用方法 |
CN107162133A (zh) * | 2017-05-26 | 2017-09-15 | 贵州美瑞特环保科技有限公司 | 一种油气田污水用功能化壳聚糖复合絮凝剂及其制备方法 |
CN108439642A (zh) * | 2018-04-16 | 2018-08-24 | 中国石油工程建设有限公司 | 一种气田水高浓度汞高效脱除系统及方法 |
CN108854972A (zh) * | 2018-06-30 | 2018-11-23 | 贵州美瑞特环保科技有限公司 | 配位聚合物增强玄武岩纤维复合材料及其制备方法 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6835311B2 (en) * | 2002-01-31 | 2004-12-28 | Koslow Technologies Corporation | Microporous filter media, filtration systems containing same, and methods of making and using |
CN106920972B (zh) * | 2017-04-11 | 2019-04-16 | 大连理工大学 | 一种基于污泥的氮掺杂生物炭和多孔火山岩的新型复合阳极的制备方法及微生物燃料电池 |
US11008234B2 (en) * | 2017-12-22 | 2021-05-18 | The Florida State University Research Foundation, Inc. | Reactors and methods for producing and recovering extracellular metal or metalloid nanoparticles |
AU2021251710A1 (en) * | 2020-04-07 | 2022-10-27 | Tessenderlo Kerley, Inc. | Removing water-soluble heavy metal-sulfur complex from process solution |
-
2021
- 2021-03-01 CN CN202110227850.5A patent/CN113000029B/zh active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6383388B1 (en) * | 1995-08-08 | 2002-05-07 | The Regents Of The University Of California | Water treatment process and system for metals removal using Saccharomyces cerevisiae |
CN103357277A (zh) * | 2013-07-24 | 2013-10-23 | 浙江师范大学 | 一种具有重金属离子吸附功能的超滤膜及其制备方法 |
WO2016125041A1 (en) * | 2015-02-03 | 2016-08-11 | Nawani Neelu | A method for removal of metals from aqueous solutions using bio adsorbents |
CN106914222A (zh) * | 2015-12-28 | 2017-07-04 | 沈阳中科环境工程科技开发有限公司 | 一种用于去除液相汞的吸附剂及其制备方法和使用方法 |
CN106237985A (zh) * | 2016-08-16 | 2016-12-21 | 四川师范大学 | 一种秸秆基选择性除汞材料及其制备方法和应用 |
CN106215845A (zh) * | 2016-08-26 | 2016-12-14 | 中国石油天然气股份有限公司 | 一种铜基脱汞吸附剂的脱汞及再生方法 |
CN107162133A (zh) * | 2017-05-26 | 2017-09-15 | 贵州美瑞特环保科技有限公司 | 一种油气田污水用功能化壳聚糖复合絮凝剂及其制备方法 |
CN108439642A (zh) * | 2018-04-16 | 2018-08-24 | 中国石油工程建设有限公司 | 一种气田水高浓度汞高效脱除系统及方法 |
CN108854972A (zh) * | 2018-06-30 | 2018-11-23 | 贵州美瑞特环保科技有限公司 | 配位聚合物增强玄武岩纤维复合材料及其制备方法 |
Non-Patent Citations (8)
Title |
---|
Adsorption affinity and selectivity of 3-ureidopropyltriethoxysilane grafted oil palm empty fruit bunches towards mercury ions;Kunjirama, M et al.;《Environmental Science And Pollution Research》;20170630;15167-15181 * |
Eggshell membrane-based solid-phase extraction combined with hydride generation atomic fluorescence spectrometry for trace arsenic(V) in environmental water samples;Zhang, YJ et al.;《Talanta》;20100315;1907-1912 * |
High removal efficacy of Hg(II) and MeHg(II) ions from aqueous solution by organoalkoxysilane-grafted lignocellulosic waste biomass;Saman, N et al.;《Chemosphere》;20170331;19-30 * |
Impact of microbial activity on the mobility of metallic elements (Fe, Al and Hg) in tropical soils;Balland-Bolou-Bi, C et al.;《Geoderma》;20190115;146-154 * |
功能性生物质材料的制备及性能研究;楚状状等;《2019第二届天然材料研究与应用研讨会论文集》;20191108;54-55 * |
气田水中汞的形态分析;严启团等;《当代化工》;20180428;848-850 * |
气田水中汞的赋存形态分析及其脱除方法;张锋等;《科学技术与工程》;20161208;320-324 * |
静电纺丝法制备具有吸附、分离及检测重金属离子功能的纳米复合纤维膜材料;魏士明;《中国优秀硕士学位论文全文数据库》;20170315;B016-700 * |
Also Published As
Publication number | Publication date |
---|---|
CN113000029A (zh) | 2021-06-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113000029B (zh) | 一种用于油气田污水中汞去除回收的生物基吸附过滤纤维膜的制备方法 | |
CN102527347B (zh) | 一种磁性壳聚糖/阳离子表面活性剂改性沸石吸附剂及其制备方法和应用 | |
CN101357325B (zh) | 一种含偕胺肟基和羧基的球形纤维素螯合吸附剂及其制备方法 | |
CN103447013B (zh) | 一种石墨烯/壳聚糖吸附剂的制备方法及其应用方法 | |
CN102500333B (zh) | 磁性阳离子表面活性剂改性壳聚糖/羟基磷灰石/沸石复合物及其制备方法和应用 | |
CN102389780B (zh) | 一种水处理剂及其制备方法 | |
CN106179249B (zh) | 一种凹凸棒纤维素复合吸附微球的制备方法 | |
CN105013447A (zh) | 一种改性纤维素重金属吸附剂的制备方法 | |
CN1803275A (zh) | 一种新型硅胶负载交联壳聚糖重金属离子吸附剂 | |
CN107744801A (zh) | 一种新型的木质素基聚酚胺吸附材料及制备方法 | |
CN107638872B (zh) | 一种粉煤灰/磁性秸秆复合材料及其制备方法与应用 | |
CN111905695A (zh) | 纤维素基中空多孔碳纤维微球吸附剂及其制备方法 | |
CN108889278B (zh) | 一种可清除汞离子的复合吸附微球的制备方法 | |
CN103464119A (zh) | 一种半胱氨酸改性棕榈树皮吸附剂的制备及应用 | |
CN108970587B (zh) | 一种复合改性蒙脱土壳聚糖交联吸附剂及其制备方法 | |
CN1754883A (zh) | 一种用水作溶剂从油茶饼粕中提取茶皂素的生产方法 | |
CN105771913A (zh) | 利用改性玉米芯净化洗脱重度石油污染土壤清洗液的方法 | |
CN101912767A (zh) | 一种改性糠醛渣重金属吸附剂的制备方法 | |
CN106861648A (zh) | 一种硫化螯合改性秸秆纤维吸附剂的制备方法及产品 | |
CN104445499A (zh) | 以柿叶为原料的金属吸附剂吸附和回收重金属镉的方法 | |
Shi et al. | Preparation of macroporous high adsorbent resin and its application for heavy metal ion removal | |
CN109718726B (zh) | 一种双亲型氧化硅-壳聚糖复合气凝胶的生产工艺 | |
CN105692845B (zh) | 一种柚子皮天然混凝剂的制备方法 | |
CN108940218B (zh) | 一种重金属吸附剂-木质素微球的制备方法 | |
CN103272570A (zh) | 一种半纤维素/壳聚糖/纳米TiO2杂化材料的制备方法及应用 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |