CN207581565U - A kind of oil field higher suspension water treatment system - Google Patents
A kind of oil field higher suspension water treatment system Download PDFInfo
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- CN207581565U CN207581565U CN201721572643.9U CN201721572643U CN207581565U CN 207581565 U CN207581565 U CN 207581565U CN 201721572643 U CN201721572643 U CN 201721572643U CN 207581565 U CN207581565 U CN 207581565U
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Abstract
本实用新型公开了一种油田高悬浮水处理系统,它包括自由水分离器(1)、合格油换热器(2)、水缓冲舱(3),合格油换热器(2)的上下端部分别设置有端口C和端口D,端口C与端口D通过管道连接,合格油换热器(2)的左右端部分别设置有端口A和端口B,端口A与端口B通过管道连接,端口B处顺次连接有原油热处理器(4)、加压泵A(5)、电脱预加热器(6)和电脱水器(7)。本实用新型的有益效果是:结构紧凑、处理效果好、能够实现油水分离、工序步骤少。
The utility model discloses an oil field high suspension water treatment system, which comprises a free water separator (1), a qualified oil heat exchanger (2), a water buffer cabin (3), and the upper and lower parts of the qualified oil heat exchanger (2). Port C and port D are respectively provided at the ends, and port C and port D are connected through pipes, and the left and right ends of the qualified oil heat exchanger (2) are respectively provided with port A and port B, and port A and port B are connected through pipes, Port B is connected in sequence with a crude oil thermal processor (4), booster pump A (5), electric dehydration pre-heater (6) and electric dehydrator (7). The beneficial effect of the utility model is that the structure is compact, the treatment effect is good, the separation of oil and water can be realized, and the process steps are few.
Description
技术领域technical field
本实用新型涉及油田高悬浮水处理的技术领域,特别是一种油田高悬浮水处理系统。The utility model relates to the technical field of oil field high suspension water treatment, in particular to an oil field high suspension water treatment system.
背景技术Background technique
油田污水主要包括原油脱出水(又名油田采出水)、钻井污水及站内其它类型的含油污水。油田污水的处理依据油田生产、环境等因素可以有多种方式。海上油田由于其本身的特殊性,在对油田污水处理过程中存在诸多困难,例如成本、场地、环保要求等等,特别是对于存在污水排海和回注的海上油田,确保处理后的污水满足排放标准和回注标准,存在一定困难。Oilfield sewage mainly includes crude oil produced water (also known as oilfield produced water), drilling sewage and other types of oily sewage in stations. There are many ways to treat oilfield sewage according to factors such as oilfield production and environment. Due to its particularity, offshore oilfields have many difficulties in the process of oilfield sewage treatment, such as cost, site, environmental protection requirements, etc., especially for offshore oilfields with sewage discharge and reinjection, to ensure that the treated sewage meets Discharge standards and reinjection standards, there are certain difficulties.
目前油田处理中心在正常生产情况下,需要确保原油处理合格,满足外输油品(含水杂﹤0.5%),同时需要满足污水处理合格(目前处理后的水中要求含油平均在10mg/l内),才能符合排海水和回注水质规定。然而,随着油田的生产,油田舱内会逐步产生难以处理的含高浓度悬浮物的污水(以下简称高悬水),该高悬水成分极其复杂,含油种类多,且由于原油和污水处理使用多种化学药剂,导致其乳化程度高,使用目前油田原有的污水处理设备要实现油水分离并达到《海洋石油开发工业含油污水排放标准》和回注标准有很大难度。At present, under normal production conditions, the oilfield treatment center needs to ensure that the crude oil treatment is qualified to meet the requirements of oil products for export (water content < 0.5%), and at the same time, it needs to meet the sewage treatment requirements (currently the oil content in the treated water is required to be within 10mg/l on average) , in order to comply with the discharge water and reinjection water quality regulations. However, with the production of oilfields, sewage containing high-concentration suspended solids (hereinafter referred to as high-suspended water) that is difficult to treat will gradually be produced in the oilfield tank. The use of a variety of chemical agents leads to a high degree of emulsification. It is very difficult to use the original sewage treatment equipment in the oilfield to achieve oil-water separation and meet the "Discharge Standards for Oily Wastewater in Offshore Oil Development Industry" and reinjection standards.
此外,随着油田综合调整项目的投产,高悬水处理问题带来的流程困扰日益显现,已经严重影响到了正常油水处理及外输作业。In addition, with the commissioning of the oilfield comprehensive adjustment project, the process troubles caused by the problem of high-hanging water treatment have become increasingly apparent, which has seriously affected the normal oil-water treatment and export operations.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术的缺点,提供一种结构紧凑、处理效果好、能够实现油水分离、工序步骤少的油田高悬浮水处理系统。The purpose of the utility model is to overcome the disadvantages of the prior art and provide an oilfield high-suspension water treatment system with compact structure, good treatment effect, oil-water separation and few process steps.
本实用新型的目的通过以下技术方案来实现:一种油田高悬浮水处理系统,它包括自由水分离器、合格油换热器、水缓冲舱,所述合格油换热器的上下端部分别设置有端口C和端口D,端口C与端口D通过管道连接,合格油换热器的左右端部分别设置有端口A和端口B,端口A与端口B通过管道连接,所述端口B处顺次连接有原油热处理器、加压泵A、电脱预加热器和电脱水器,电脱预加热器的底部设置有含油污水出口,该含油污水出口与水缓冲舱连接,电脱预加热器的顶部设置有排气口I,排气口I处连接有燃烧罐,电脱水器的合格油出口与端口C连接,所述端口A与自由水分离器的含水原油出口端连接,自由水分离器的顶部设置有排气口II,自由水分离器的底部设置有含油污水出口,该含油污水出口与水缓冲舱连接,水缓冲舱的出口处顺次连接有加压泵B、斜板除油器、加气浮选器、加压泵C和核桃壳过滤器。The purpose of this utility model is achieved through the following technical solutions: a high-suspension water treatment system in an oil field, which includes a free water separator, a qualified oil heat exchanger, and a water buffer cabin, and the upper and lower ends of the qualified oil heat exchanger are respectively Port C and port D are provided, and port C and port D are connected by pipes. The left and right ends of the qualified oil heat exchanger are respectively provided with port A and port B. Port A and port B are connected by pipes. The crude oil heat processor, booster pump A, electric pre-heater and electric dehydrator are connected for the second time. The bottom of the electric pre-heater is provided with an oily sewage outlet, and the oily sewage outlet is connected with the water buffer tank. The electric pre-heater The top of the tank is provided with an exhaust port I, and the combustion tank is connected to the exhaust port I, and the qualified oil outlet of the electric dehydrator is connected to port C, and the port A is connected to the water-containing crude oil outlet end of the free water separator, and the free water is separated The top of the separator is provided with an exhaust port II, and the bottom of the free water separator is provided with an oily sewage outlet, which is connected to the water buffer tank, and the outlet of the water buffer tank is connected with a booster pump B and a sloping plate removal tank in sequence. oiler, air flotation unit, booster pump C and walnut shell filter.
所述的排气口II处顺次连接有燃气压缩器。A gas compressor is sequentially connected to the exhaust port II.
所述的燃气压缩器与燃烧罐连接。The gas compressor is connected with the combustion tank.
所述端口D处连接有货油舱。The port D is connected to a cargo oil tank.
本实用新型具有以下优点:本实用新型结构紧凑、处理效果好、能够实现油水分离、工序步骤少。The utility model has the following advantages: the utility model has compact structure, good treatment effect, can realize oil-water separation, and has few process steps.
附图说明Description of drawings
图1 为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图中,1-自由水分离器,2-合格油换热器,3-水缓冲舱,4-原油热处理器,5-加压泵A,6-电脱预加热器,7-电脱水器,8-加压泵B,9-斜板除油器,10-加气浮选器,11-加压泵C,12-核桃壳过滤器,13-燃气压缩器,14-燃烧罐。In the figure, 1-free water separator, 2-qualified oil heat exchanger, 3-water buffer tank, 4-crude oil heat processor, 5-boosting pump A, 6-electric preheater, 7-electric dehydrator , 8-pressurization pump B, 9-slope plate oil remover, 10-gas flotation device, 11-pressurization pump C, 12-walnut shell filter, 13-gas compressor, 14-combustion tank.
具体实施方式Detailed ways
下面结合附图对本实用新型做进一步的描述,本实用新型的保护范围不局限于以下所述:Below in conjunction with accompanying drawing, the utility model is further described, and the protection scope of the utility model is not limited to the following:
如图1所示,一种油田高悬浮水处理系统,它包括自由水分离器1、合格油换热器2、水缓冲舱3,所述合格油换热器2的上下端部分别设置有端口C和端口D,端口C与端口D通过管道连接,合格油换热器2的左右端部分别设置有端口A和端口B,端口A与端口B通过管道连接,所述端口B处顺次连接有原油热处理器4、加压泵A5、电脱预加热器6和电脱水器7,电脱预加热器6的底部设置有含油污水出口,该含油污水出口与水缓冲舱3连接,电脱预加热器6的顶部设置有排气口I,排气口I处连接有燃烧罐14,电脱水器7的合格油出口与端口C连接。端口D处连接有货油舱As shown in Figure 1, a kind of oil field high suspension water treatment system, it comprises free water separator 1, qualified oil heat exchanger 2, water buffer cabin 3, the upper and lower ends of described qualified oil heat exchanger 2 are respectively provided with Port C and port D, port C and port D are connected through pipelines, the left and right ends of the qualified oil heat exchanger 2 are respectively provided with port A and port B, port A and port B are connected through pipelines, and the ports at B are sequentially Connected with crude oil heat processor 4, pressurization pump A5, electric pre-heater 6 and electric dehydrator 7, the bottom of electric pre-heater 6 is provided with oily sewage outlet, the oily sewage outlet is connected with water buffer cabin 3, electric The top of the pre-heater 6 is provided with an exhaust port 1, and the exhaust port 1 is connected with a combustion tank 14, and the qualified oil outlet of the electric dehydrator 7 is connected with the port C. Cargo tank is connected at port D
如图1所示,所述端口A与自由水分离器1的含水原油出口端连接,自由水分离器1的顶部设置有排气口II,自由水分离器1的底部设置有含油污水出口,该含油污水出口与水缓冲舱3连接,水缓冲舱3的出口处顺次连接有加压泵B8、斜板除油器9、加气浮选器10、加压泵C11和核桃壳过滤器12。所述的排气口II处顺次连接有燃气压缩器13,所述的燃气压缩器13与燃烧罐14连接。As shown in Figure 1, the port A is connected to the water-containing crude oil outlet end of the free water separator 1, the top of the free water separator 1 is provided with an exhaust port II, and the bottom of the free water separator 1 is provided with an oily sewage outlet, The oily sewage outlet is connected to the water buffer cabin 3, and the outlet of the water buffer cabin 3 is connected with a booster pump B8, an inclined plate degreaser 9, an air flotation device 10, a booster pump C11 and a walnut shell filter 12. A gas compressor 13 is sequentially connected to the exhaust port II, and the gas compressor 13 is connected to a combustion tank 14 .
本实用新型的工作过程如下:将油田舱中含高浓度悬浮物的污水泵入自由水分离器1中,自由水分离器1分离出含水原油、含油污水和气体,其中气体被燃气压缩器13压缩后进入燃烧罐14中燃烧,含油污水进入水缓冲舱3中收集,含水原油经端口A后从端口B流出,流出后进入原油热处理器4;原油热处理器4将含水原油加热到75~93℃,原油热处理器4分离出含水原油、含油污水和气体,其中气体进入燃烧罐14中燃烧,含油污水进入水缓冲舱3中收集,而分离出的含水原油经加压泵A5泵入电脱预加热器6中,电脱预加热器6将含水原油加热到100~125℃,加热后进入电脱水器7中,电脱水器7分离出的合格原油,合格的原油经端口C进入合格油换热器2中,使合格原油与从自由水分离器1分离出的含水原油进行热交换,热交换后产品经端口D进入货油舱中,由货油舱向外输油;水缓冲舱3中的含油污水经加压泵B8泵入斜板除油器9中,斜板除油器9将污水中较大的颗粒从水中分离出来,在压差作用下经处理后的含油污水被送至加气浮选器10中,加气浮选器10通过加气浮选法除去污水中的乳化油和更小的悬浮颗粒,经处理后经加压泵C11泵入核桃壳过滤器12中,核桃壳过滤器12滤掉污水中4微米以上的悬浮固体颗粒,最终得到含油量低于7~15ppm的水,符合污水排放标准,实现了油水分离,解决了高悬水处理困难的问题,促进了油水处理及外输作业的正常进行。The working process of the utility model is as follows: the sewage containing high-concentration suspended solids in the oil field tank is pumped into the free water separator 1, and the free water separator 1 separates water-containing crude oil, oil-containing sewage and gas, wherein the gas is pumped by the gas compressor 13 After being compressed, it enters the combustion tank 14 for combustion, and the oily sewage enters the water buffer tank 3 for collection. The watery crude oil flows out from the port B after passing through the port A, and then enters the crude oil heat processor 4 after flowing out; the crude oil heat processor 4 heats the watery crude oil to 75~93 ℃, the crude oil thermal processor 4 separates water-containing crude oil, oil-containing sewage and gas, wherein the gas enters the combustion tank 14 for combustion, and the oil-containing sewage enters the water buffer tank 3 for collection, and the separated water-containing crude oil is pumped into the electric degasser through the booster pump A5. In the pre-heater 6, the electric pre-heater 6 heats the water-containing crude oil to 100~125°C, and enters the electric dehydrator 7 after heating. The qualified crude oil separated by the electric dehydrator 7 enters the qualified crude oil through port C. In the heat exchanger 2, the qualified crude oil is subjected to heat exchange with the water-containing crude oil separated from the free water separator 1. After the heat exchange, the product enters the cargo oil tank through port D, and the oil is transported from the cargo oil tank to the outside; the water buffer tank The oily sewage in 3 is pumped into the inclined plate degreaser 9 through the booster pump B8, and the inclined plate degreaser 9 separates the larger particles in the sewage from the water, and the treated oily sewage is discharged under the action of pressure difference. Sent to the air flotation device 10, the air flotation device 10 removes the emulsified oil and smaller suspended particles in the sewage by the air flotation method, and after treatment, it is pumped into the walnut shell filter 12 by the booster pump C11 Among them, the walnut shell filter 12 filters out suspended solid particles above 4 microns in the sewage, and finally obtains water with an oil content of less than 7-15ppm, which meets the sewage discharge standard, realizes the separation of oil and water, and solves the problem of difficult treatment of high suspended water , Promote the normal operation of oil and water treatment and export operations.
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CN112908138A (en) * | 2019-12-03 | 2021-06-04 | 中国海洋石油集团有限公司 | Floating type oil-water replacement storage and discharge platform pool test device and operation method |
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CN112908138A (en) * | 2019-12-03 | 2021-06-04 | 中国海洋石油集团有限公司 | Floating type oil-water replacement storage and discharge platform pool test device and operation method |
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