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INNOVATIVE LOW TEMPERATURE BREAKER SYSTEM SUITABLE FOR FRACTURING ULTRA LOW TEMPERATURE INDIAN RESERVOIRS

机译:适用于压裂印度洋超低温储层的新型低温破碎机系统

摘要

A formulation and a process for preparing hydraulic fracturing fluid suitable for carrying out fracturing in wells having ultra low temperatures and shallow reservoirs, the process comprising the steps of taking sea water in a pre-cleaned gel storage tank and adding 0.03 wt % Biocide to the tank during filling of water; mixing to the tank a 2-4 wt % Clay Hydration Suppressant with constant agitation with the help of a blender unit; characterized in that in the subsequent steps, 0.5 wt % water softener from group consisting salt of amino-poly carboxylic acid is added to the tank while at constant agitation with the help of same blender unit; and wherein pH of solution in the tank at this stage is adjusted to = 8.50 by adding 0.4-0.45 wt % soda ash; adding 0.60-0.70 wt % gelling agent Gd.-II in the same blender unit having the facility of dry chemical mixing fitted with high rate water jetting system; and wherein after mixing and homogenizing of the required amount of the gelling agent into the tank through the blender unit, 0.04 wt % of ammonium persulphate is mixed to the tank with the help of the blender unit; adjusting the pH of the tank to = 7 by adding 0.13-0.15 vol % of acetic acid through the blender; adding 0.50% oil specific non-emulsifier and 0.5 wt % of surfactant to the tank with help of the blender unit; allowing sufficient hydration time by keeping the neutral linear gel in the tank on agitation/circulation mode and when the gel in tank attains the required gel viscosity of 40 cps (at 511 s-1), adding and mixing thoroughly 0.35-0.45 wt % soda ash to the blender unit to raise the pH of the base gel to = 9.5; adding to the gel tank and mixing thoroughly 0.04 wt % of SA-102; and wherein 0.06 wt % of APS + 0.06 wt % of SA-102 and 0.04-0.05 wt % of borax is mixed on the fly.
机译:适于在具有超低温和浅储层的井中进行压裂的水力压裂液的制剂和方法,该方法包括以下步骤:将海水吸入预先清洁的凝胶储罐中,并向其中添加0.03 wt%的杀菌剂。装满水时的水箱;在搅拌器的帮助下,在不断搅拌下将2-4 wt%的粘土水化抑制剂混合到罐中;其特征在于,在随后的步骤中,在相同搅拌器的帮助下,在不断搅拌下,将0.5重量%的氨基-多羧酸盐组成的组的水软化剂加入到该罐中。并且其中通过添加0.4-0.45重量%的苏打灰将在该阶段的罐中溶液的pH调节至= 8.50;在具有干式化学混合设备并装有高速水喷射系统的同一搅拌器单元中,添加0.60-0.70 wt%的胶凝剂Gd.-II;其中通过混合器单元将所需量的胶凝剂混合并均化到罐中后,借助于搅拌器单元将0.04重量%的过硫酸铵混合到罐中;通过搅拌器加入0.13-0.15%(体积)的乙酸,将罐的pH调节至= 7。在搅拌器单元的帮助下,向罐中添加0.50%的油性非乳化剂和0.5 wt%的表面活性剂;通过在搅拌/循环模式下将罐中的中性线性凝胶保持在罐中的凝胶达到所需的40 cps凝胶粘度(在511 s-1时),充分添加和混合0.35-0.45 wt%的苏打,从而允许充足的水化时间灰至混合器单元以将基础凝胶的pH提高至9.5;加入凝胶罐中并充分混合0.04重量%的SA-102;并且其中0.06重量%的APS + 0.06重量%的SA-102和0.04-0.05重量%的硼砂在飞行中混合。

著录项

  • 公开/公告号IN201611009488A

    专利类型

  • 公开/公告日2018-01-26

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN201611009488

  • 申请日2016-03-18

  • 分类号C09K8/706;

  • 国家 IN

  • 入库时间 2022-08-21 12:52:16

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