JP2013215686A - Method and apparatus for treating accompaniment water from winze - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method that can treat and reuse accompaniment water by little electric power and energy.SOLUTION: A water treatment method includes: a filtration treatment process in which accompaniment water exhausted from a winze is performed by filtration process to obtain filtered water; a forward osmosis process in which the filtered water and an induction solution containing a volatile solute and having higher osmosis than that of the filtered water are contacted through a semipermeable membrane, and water in the filtered water is moved into the induction solution through the semipermeable membrane to obtain a diluted induction solution diluted by water and a membrane concentration water; a first evaporation process in which the diluted induction solution is heated, gas consisting of the volatilized solute and water vapor is obtained and purified water that hardly contains the solute is obtained; a regeneration process in which the gas is cooled to regenerate the induction solution; a second evaporation process in which the membrane concentration water obtained by the forward osmosis process is subjected to evaporation/concentration to obtain evaporation/concentration water and condensed water; and a crystallization process in which the evaporation/concentration water is further subjected to evaporation/concentration and salts contained in the evaporation/concentration water are precipitated and condensed water is obtained.

Description

  The present invention relates to a method for treating associated water produced when mining natural gas or crude oil from a well such as shale gas, oil sand, CBM (coal bed methane), or oil.

  When mining shale gas, oil sand, CBM (coal bed methane), petroleum, etc., an aqueous chemical solution may be injected as drilling water or steam to increase the amount of natural gas or crude oil. As a result, the crude oil extracted from the oil reservoir contains these chemical aqueous solutions and groundwater containing inorganic ions in the formation as associated water, and the associated water is separated from the mined natural gas and crude oil. Since the separated associated water contains salt, organic matter, suspension, etc., if it is discharged as it is, it causes environmental pollution problems and needs to be purified.

  As a technique for purifying the accompanying water, a technique has been developed in which suspended solids and organic substances are removed by sand filtration and activated carbon treatment and discharged into the ocean while leaving the salt content (Patent Document 1).

  A technique using membrane separation is also known (Patent Document 2). The method first converts the water-soluble silica contained in the accompanying water into a suspension of insoluble silica, removes it with a ceramic membrane, then evaporates and recovers water with an evaporator and reuses it for crude oil mining. It is to do. The use of a reverse osmosis membrane instead of the evaporator is also disclosed.

Japanese Patent Application Laid-Open No. 2004-275484 US Patent Application Publication No. 2011/0168629 A1 (page 3, FIG. 3)

  The technique using the membrane separation of Patent Document 2 is excellent in that the accompanying water can be purified and reused, but the reverse osmosis membrane treatment is performed at a high pressure of about 6 to 8 MPa and requires a large amount of power. Further, a large amount of the concentrated water remaining without passing through the reverse osmosis membrane is generated in about half of the accompanying water, and energy is also required for evaporation of the concentrated water.

  An object of the present invention is to provide a method capable of treating and reusing the accompanying water with less power and energy.

  The present invention has been made to solve the above-mentioned problems. By performing the forward osmosis membrane treatment instead of the reverse osmosis membrane treatment, the power required to pressurize to a high pressure is eliminated, and the forward osmosis membrane treatment is changed. The total power required for the treatment of the associated water is obtained by using the heat of the condensate generated in the subsequent crystallization process as the heat source for heating the diluted induction solution required for the evaporation. It has been found that the amount and energy can be saved and the present invention has been completed.

That is, the present invention
(1) Filtration treatment of accompanying water discharged from a well to obtain filtrate water, the filtrate water, a volatile solute, and a higher osmotic pressure induction solution than the filtrate water. A forward osmosis step of contacting the membrane through a semipermeable membrane, transferring the water in the filtered water to the induction solution through the semipermeable membrane to obtain a diluted induction solution diluted with water and membrane concentrated water, and the dilution induction solution To obtain a gas composed of the solute and water vapor that has volatilized, and obtain purified water containing almost no solute, and a regeneration step of regenerating the induction solution by cooling the gas, Evaporating and concentrating the membrane concentrated water obtained in the forward osmosis step to obtain evaporated concentrated water and condensed water, further evaporating and concentrating the evaporated concentrated water, and depositing salts contained in the evaporated concentrated water And a crystallization process for obtaining condensed water. A water treatment method characterized by,
(2) At least one of the condensed water obtained in the second evaporation step and the condensed water obtained in the crystallization step is used as a heating source for the diluted induction solution in the first evaporation step (1) A water treatment method as described in
(3) At least one of the condensed water obtained in the second evaporation step and the condensed water obtained in the crystallization step is directly introduced as a heating source into the diluted induction solution in the first evaporation step (2) ) Water treatment method according to
(4) The water treatment method according to any one of (1) to (3), wherein the purified water is reused as drilling water or steam for the well.
(5) Filtration of the associated water discharged from the well to obtain filtered water, the filtered water, a volatile solute, and a osmotic pressure induction solution higher than the filtered water. A forward osmosis membrane treatment device that makes contact through a permeable membrane, moves water in the filtered water to the induction solution through the semipermeable membrane, and obtains a diluted induction solution diluted with water and membrane concentrated water, and the dilution induction A first evaporator that heats the solution to obtain a gas composed of the volatilized solute and water vapor, and obtains purified water that hardly contains the solute; a heat exchanger that cools the gas and regenerates the induction solution; A second evaporation device for evaporating and concentrating the membrane concentrated water obtained from the forward osmosis treatment device to obtain evaporated concentrated water and condensed water, and further evaporating and concentrating the evaporated concentrated water, and salts contained in the evaporated concentrated water And a crystallizer to obtain condensed water A water treatment apparatus which is characterized in that,
(6) Provided with means for directly introducing at least one of the condensed water obtained from the second evaporator and the condensed water obtained from the crystallizer as a heating source into the dilution induction solution in the first evaporator. The water treatment device according to (5), which is characterized, is provided.

  According to the present invention, accompanying water discharged from a well can be treated with less electric power and energy, and the treated water can be reused as drilling water or steam.

It is a figure which shows schematic structure of the apparatus of this invention.

  The well to which the present invention is applied is not particularly limited as long as it discharges accompanying water, and is, for example, a well for mining shale gas, oil sand, CBM (coal bed methane), oil, or the like.

Accompanying water is water that is discharged along with the object to be mined from the well, and includes salt, organic matter, suspended matter, and the like. Concentrations of pollutants include, for example, evaporation residues (mainly Na ⁺ , K ⁺ , Ca ²⁺ , Cl ⁻ , SO ₄ ^2−, etc.) of 1,000 to 100,000 mg / L, organic substances (such as oil and added chemicals) Is contained in a range of 10 to 1,000 mg / L as TOC and suspended material in a range of 100 to 10,000 mg / L.

  Although the accompanying water separation means is not limited, for example, oil-water separation is performed by sedimentation or the like.

Filtration process In this invention, this separated accompanying water is first filtered. This filtration treatment is performed with a filter using a microfiltration membrane, and a normal membrane used as a microfiltration membrane can be used as the filtration membrane. For example, in addition to cellulose acetate, polytetrafluoroethylene, polysulfone, polyvinyl chloride, etc., ceramic membranes and porous glass membranes can also be used. In the micromembrane filtration treatment, membrane filtrate water that has passed through the microfiltration membrane and membrane concentrated water remaining without passing through the membrane are obtained.
In addition to precision membrane filtration, filtration treatment such as ultramembrane filtration and sand filtration is used. The material for the ultrafiltration is the same as that for precision membrane filtration.

Forward osmosis process Next, this membrane filtrate is processed by the forward osmosis method.

  The forward osmosis method is a method in which the membrane filtrate and an induction solution having a higher osmotic pressure than the membrane filtrate are brought into contact with each other through a semipermeable membrane, and the water in the membrane filtrate is transferred to the induction solution through the semipermeable membrane. A semipermeable membrane device is used.

The induction solution is an aqueous solution having an osmotic pressure higher than that of the membrane filtrate, for example, an aqueous ammonium carbonate solution formed by dissolving a predetermined amount of ammonia and carbon dioxide in water. The predetermined amount is an amount that makes the water in the membrane filtrate pass through the semipermeable membrane and move to the induction solution, so that the osmotic pressure of the induction solution is higher than the osmotic pressure of the membrane filtration water. Is set. When using an aqueous ammonium carbonate solution, the upper limit of the concentration is determined so that a salt of ammonia and carbon dioxide, that is, ammonium carbonate, ammonium hydrogen carbonate, ammonium carbamate, etc. does not precipitate on the semipermeable membrane surface or in the distillation column. Can be determined by experiment. One of the methods for confirming whether or not precipitates are generated on the semipermeable membrane surface or in the distillation column is a method of judging whether stable operation is possible by operating for a long time. The molar ratio of ammonia to carbon dioxide is about 1.5-3. This molar ratio is also taken into consideration so that salts of ammonia and carbon dioxide do not precipitate on the semipermeable membrane surface or in the first evaporator.
As the solute of the induction solution, in addition, it is possible to use a high solubility, high osmotic pressure, low boiling point, high volatility and low toxicity. For example, alcohols such as ethyl alcohol and butyl alcohol And ketones such as acetone can also be used.

  The semipermeable membrane is preferably one that can selectively permeate water and is preferably a forward osmosis membrane, but a reverse osmosis membrane can also be used. The material is not particularly limited, and examples thereof include cellulose acetate-based, polyamide-based, polyethyleneimine-based, polysulfone-based, and polybenzimidazole-based materials. The form of the semipermeable membrane is not particularly limited and may be any of a flat membrane, a tubular membrane, a hollow fiber, and the like.

  A device for mounting this semipermeable membrane is usually a semi-permeable membrane installed in a cylindrical or box-shaped container, and membrane filtered water flows into one chamber partitioned by this semipermeable membrane, and the other chamber is filled with water. The induction solution can be flowed, and a known semipermeable membrane device can be used, and a commercially available product can be used.

  The inlet of the chamber through which the membrane filtrate flows is connected to the membrane filtrate outlet of the precision membrane filtration device or its reservoir, if any. The outlet side is connected by piping to the inlet of the second evaporator. A circulating line connecting both pipes can be provided to circulate the membrane filtrate.

  The inlet of the chamber through which the induction solution flows is piped to the heat exchanger outlet of the regeneration process, and the outlet is piped to the inlet side of the first evaporator, thereby forming a circulation line for the induction solution.

First evaporation step The first evaporation step is a step of heating the diluted induction solution obtained in the forward osmosis step to obtain a gas composed of volatilized solute and water vapor and obtaining purified water containing almost no solute of the induction solution. In the first evaporator, a distillation column can be used.

  A known distillation column may be used, and any type such as a shelf system and a packing system may be used. A heater is provided at the lower part of the distillation tower, and the steam generated by heating the purified water at the lower part is brought into contact with the diluted induction solution falling from the upper part to exchange heat. A reboiler, a heat exchanger, etc. can be used for a heater. Regardless of the heat source of the heater, either or both of the condensed water obtained in the second evaporation step and the condensed water obtained in the crystallization step can be used as a heat source, and these are directly fed to the first evaporator. It is also possible to eliminate losses due to heat exchange. This method is applied when the evaporation temperature in the first evaporation step is lower than the condensed water temperature in the second evaporation step.

  The first evaporator is provided with a diluting induction solution inlet, a gas outlet consisting of the solute and water vapor of the induction solution volatilized by heating, and a remaining purified water outlet. The outlet of the diluting induction solution of the forward osmosis membrane treatment apparatus, the gas outlet is connected to a heat exchanger for the regeneration process, and the purified water outlet is connected to a water purification tank or a water tank for excavation.

Regeneration step The regeneration step is a step of regenerating the induction solution by cooling the gas, and a heat exchanger is used. A dilution induction solution discharged from the forward osmosis membrane treatment apparatus or the like can be used as the heat source for cooling. The regenerated induction solution is reused in the forward osmosis process.

Second evaporation step The second evaporation step is a step of evaporating and concentrating the membrane concentrated water obtained in the filtration step and the membrane concentrated water obtained in the forward osmosis step to obtain evaporated concentrated water and condensed water. A normal evaporator, that is, a single can, a multi-effect can, a vapor compression evaporator, a multistage flash evaporator, etc. can be used for the double evaporator. Evaporation may be performed at normal pressure or reduced pressure depending on the heat source. It is preferable that the condensed water is directly supplied to the first evaporator, or the heat contained therein is used as a heat source in the first evaporation step via a heat exchanger or the like. The evaporated concentrated water is sent to the next step.

Crystallization step The crystallization step is a step of further evaporating and concentrating the evaporated concentrated water to precipitate the salts contained in the evaporated concentrated water and obtaining condensed water. Crystallization cans can be used. The condensed water is preferably used as a heat source in the first evaporation step in the same manner as the condensed water in the previous step. On the other hand, the slurry taken out from the crystallizer is separated into individual liquids, and the mother liquor containing crystals and organic substances is disposed of as industrial waste, or if it contains almost no environmental pollution components such as heavy metals and organic substances, a snow melting agent. Etc. can also be used.

  An example of the implementation of the present invention will be described with reference to FIG. The apparatus of FIG. 1 includes a reaction tank, an MF membrane (precision membrane filtration device), an FO membrane (forward osmosis membrane treatment device), an evaporator (first evaporation device), an evaporation device (second evaporation device), and a crystallizer. Arranged in this order.

The accompanying water of 1,000 m ³ / d separated from the crude oil taken out from the operating well is first put into the reaction tank, where a dispersing agent is added to suppress the precipitation of Ca ²⁺ , and then to the MF membrane. Sent. In the MF membrane, the solids contained in the accompanying water are removed as membrane concentrated water, and the membrane filtrate passing through the membrane is sent to the FO membrane. There, the induction solution contacts with the membrane, and the water contained in the membrane filtered water passes through the membrane to dilute the induction solution. This dilution induction solution enters an evaporator whose pressure is reduced to 10 kPa, and is heated there to evaporate a gas composed of carbon dioxide, ammonia and water vapor at a boiling point of 45 ° C. The amount of heat required for this evaporation is 250 GJ / d. This gas is cooled through the heat exchanger, returned to the induction solution, and returned to the FO membrane. At this time, if the accompanying water or MF filtered water is used as the cooling water, it is preferable that the effect of increasing the membrane filtration rate accompanying the decrease in viscosity due to the heating of the water to be treated is obtained. The purified water at 45 ° C. remaining in the evaporator is taken out at 1,000 m ³ / d, added with chemicals, and reused as drilling water.

On the other hand, the membrane concentrated water concentrated by the separation of water through the forward osmosis membrane is sent to the evaporator at 500 m ³ / d. The inside of this evaporator is reduced to 39 kPa by a vacuum pump, and a circulation line is formed by a heat pump, and steam is heated in the middle to heat the inside. Condensed water at 75 ° C. is separated from the evaporator and withdrawn at 250 m ³ / d.

Evaporated concentrated water collected at the bottom of the evaporator is drawn out by a pump, a part is sprayed back from the top of the evaporator, and a part is sent to the crystallizer at 250 m ³ / d as evaporated concentrated water. It is done. The crystallizer is provided with a heating mechanism that is extracted by a pump, heated by a heater, and returned, so that the internal evaporated concentrated water is further evaporated and concentrated. Salt crystals precipitated by concentration are extracted from the bottom of the crystallizer. On the other hand, the evaporated condensed water is extracted at 250 m ³ / d, heated to 75 ° C. with a heater, and then merged with the 250 m ³ / d condensed water from the evaporator, and 75 ° C. condensed water is 500 m ³ / d. It is sent to the evaporator at (63 GJ / d) and the heat is used. Insufficient heat (187 GJ / d) is further added to the evaporator as steam.

  The steam reduction effect by using the heat of the condensed water as waste heat is as follows.

この廃熱利用による蒸気削減は２５％である。

Steam reduction by using this waste heat is 25%.

Industrial application fields

  According to the present invention, accompanying water discharged together with crude oil or the like from a well such as an oil well can be treated and reused, so that it can be widely used in wells in various places.

Claims (6)

  Filtration treatment of the accompanying water discharged from the well and obtaining filtration water, the filtration water, a volatile solute, and a osmotic pressure induction solution higher than the filtration water. A forward osmosis step of transferring the water in the filtered water to the induction solution through the semipermeable membrane to obtain a diluted induction solution and membrane concentrated water diluted with water, and heating the dilution induction solution. A first evaporation step to obtain a gas composed of the volatilized solute and water vapor and obtain purified water containing almost no solute, a regeneration step to cool the gas and regenerate the induction solution, and a forward osmosis step A second evaporation step for evaporating and concentrating the membrane concentrated water obtained in step 1 to obtain evaporated concentrated water and condensed water; further evaporating and concentrating the evaporated concentrated water to precipitate salts contained in the evaporated concentrated water and condensing water; A crystallization process to obtain Water treatment method to be.   The condensed water obtained in the second evaporation step and at least one of the condensed water obtained in the crystallization step are used as a heating source for the dilution induction solution in the first evaporation step. Water treatment method.   The condensed water obtained in the second evaporation step and the condensed water obtained in the crystallization step are directly introduced as a heating source into the dilution induction solution in the first evaporation step. Water treatment method.   The water treatment method according to any one of claims 1 to 3, wherein the purified water is reused as water for drilling or steam in the well.   Filtering the accompanying water discharged from the well to obtain filtered water, the filtered water, containing a volatile solute, and a osmotic pressure induction solution higher than the filtered water through a semipermeable membrane A forward osmosis membrane treatment apparatus for obtaining a diluted induction solution diluted with water and membrane concentrated water, and heating the diluted induction solution. A first evaporator for obtaining a gas comprising the volatilized solute and water vapor and obtaining purified water containing substantially no solute; a heat exchanger for cooling the gas and regenerating the induction solution; A second evaporator for evaporating and concentrating the membrane concentrated water obtained from the permeation treatment device to obtain evaporated concentrated water and condensed water, and further evaporating and concentrating the evaporated concentrated water to precipitate salts contained in the evaporated concentrated water. And a crystallizer for obtaining condensed water Water treatment device according to claim and.   Means is provided for directly introducing at least one of the condensed water obtained from the second evaporator and the condensed water obtained from the crystallizer as a heating source into the dilution induction solution in the first evaporator. The water treatment apparatus according to claim 5.

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