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A steam injection boiler high temperature separation water reuse treatment system and treatment method

A technology of steam injection boiler and treatment system, applied in the field of high temperature separation water reuse treatment system of steam injection boiler, can solve the problems of large amount of cooling water, poor economy, blockage of traditional membrane process, etc., to reduce heat loss, ensure quality requirements, The effect of ensuring water quality

Active Publication Date: 2020-06-19
XI AN JIAOTONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 2) Steam injection boilers are rich in silicon, which can easily cause blockage of traditional membrane processes
At the same time, the membrane process requires the temperature of the treated water to be 30~40°C. Using the membrane process not only requires a large amount of cooling water, but also the heat energy in the high-temperature and high-salt separated water generated in the steam injection boiler cannot be effectively utilized as a resource, and the economy is poor.

Method used

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  • A steam injection boiler high temperature separation water reuse treatment system and treatment method

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0060] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler produces secondary steam at a temperature of about 140°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 140°C. The flash condensate produced by the steamer is about 60% of the high temperature separated water;

[0061] 2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit together with the secondary steam generated by the crystallization separation unit;

[0062] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal wastewater and boiler feed water, and then enters the regulating pool at a temperature of about 80°C, and adjusts the pH in the regulating pool to 7~10;

[0063] 4) The adjustment t...

Embodiment 2

[0070] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler produces secondary steam at a temperature of about 160°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 160°C. The flash condensate produced by the steamer is about 50% of the high temperature separated water;

[0071]2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit together with the secondary steam generated by the crystallization separation unit;

[0072] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal wastewater and boiler feed water, and then enters the regulating tank at a temperature of about 65°C, and adjusts the pH in the regulating tank to 7~10;

[0073] 4) The adjustment ta...

Embodiment 3

[0080] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler produces secondary steam at a temperature of about 160°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 160°C. The flash condensate produced by the steamer is about 50% of the high temperature separated water;

[0081] 2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit together with the secondary steam generated by the crystallization separation unit;

[0082] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal wastewater and boiler feed water, and then enters the regulating tank at a temperature of about 65°C, and adjusts the pH in the regulating tank to 7~10;

[0083] 4) The adjustment t...

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Abstract

The invention discloses a reuse treatment system and treatment method for high-temperature separated water of a steam injection boiler, and belongs to the technical field of water treatment. The system comprises the steam injection boiler, a four-stage heat exchange unit, a chemical silicon removal unit, a flash tank, a TVC unit, a buffer tank, a boiler feed water tank, and a crystallization separation unit; the fourth-stage heat exchange unit comprises a first heat exchanger, a second heat exchanger, a third heat exchanger, and a fourth heat exchanger. After silicon, salt and organic mattersare removed from the high-temperature and high-salt separated water of the steam injection boiler, the separated water is returned to the steam injection boiler, so that the quality of dry steam generated by the steam injection boiler meets the requirement of steam injection production; moreover, the waste water and the heat energy contained therein are recycled, so that cooling water is used little or not used, and near zero emission disposal and low-cost operation of the high-temperature and high-salt separated water of the steam injection boiler are achieved. The system and the method improve the ecological environment, and are of great significance on energy conservation, water conservation and sustainable use of the auxiliary gravity drainage technology.

Description

technical field [0001] The invention belongs to the field of water treatment, and in particular relates to a high-temperature separation water reuse treatment system and treatment method of a steam injection boiler. Background technique [0002] In 1978, Dr. R.M.Bulter, based on the principle of water injection and salt extraction, combined heat conduction and fluid heat convection, steam as a heat source, and relied on the gravity of asphalt and condensate to mine heavy oil, proposed the auxiliary gravity drainage for extra heavy oil development technology. Thermal recovery of heavy oil is currently the main technical means for the development of unconventional heavy oil. It has been widely used in the United States, Venezuela, and Canada. my country has successively promoted and applied it in heavy oil fields such as Liaohe, Xinjiang, Shengli, and Henan. [0003] The steam injection boiler provides a heat source for the heavy oil recovery technology, which is a very impor...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/10
CPCC02F1/06C02F1/24C02F1/60C02F9/00C02F11/121C02F2001/5218C02F2209/02C02F2209/06C02F2303/10
Inventor 王树众雷杰景泽峰杨闯徐甜甜赵军
Owner XI AN JIAOTONG UNIV
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