CN212741038U - Gasification black water treatment device - Google Patents
Gasification black water treatment device Download PDFInfo
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- CN212741038U CN212741038U CN202020965771.5U CN202020965771U CN212741038U CN 212741038 U CN212741038 U CN 212741038U CN 202020965771 U CN202020965771 U CN 202020965771U CN 212741038 U CN212741038 U CN 212741038U
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Abstract
The utility model discloses a gasification black water treatment device, which relates to the field of coal gasification black water treatment; the device comprises a primary flash tank, a secondary flash tank, a tertiary flash tank, a settling tank, an ammonia distillation tower and a hot water tower, wherein a water outlet of the primary flash tank is communicated with the secondary flash tank; the utility model discloses can effectively desorption gasification suspended solid, hardness, three types of materials of ammonia nitrogen in the black water to realize reducing device demineralized water quantity and waste water discharge, alleviate equipment pipeline deposition scale deposit, extension device operating cycle's purpose has saved the water resource simultaneously and has protected more the environment.
Description
Technical Field
The utility model discloses a gasification black water treatment device, which relates to the field of coal gasification black water treatment, in particular to a gasification black water treatment device.
Background
At present, no matter the water coal slurry process or the dry coal powder gasification process, the crude synthesis gas generated by the gasification furnace needs to be washed by water bath to remove solid particles of the synthesis gas. In the course of washing the crude synthesis gas, because the washing water consumption is large, at present, the black water produced after washing the crude synthesis gas is usually returned to the system for repeated use after flash evaporation and sedimentation treatment, so as to save resources, but soluble substances containing elements such as calcium, magnesium, nitrogen and the like in solid particles are dissolved in the washing water, so that the washed black water is easy to scale and the ammonia nitrogen content is increased, which is not beneficial to washing the crude synthesis gas. Although solid particles in black water can be removed by flash evaporation and sedimentation technologies in the existing black water treatment technologies, the content of ammonia nitrogen and calcium and magnesium ions in the black water cannot be effectively reduced, and if the quality of the washed black water is stabilized by supplementing a large amount of desalted water and discharging high-hardness and high-ammonia nitrogen wastewater, the burden of a sewage treatment system must be increased, and particularly, the impact on the sewage treatment system is aggravated when the coal quality of a gasification furnace fluctuates.
SUMMERY OF THE UTILITY MODEL
The utility model discloses to prior art's problem, provide a gasification black water processing apparatus, can effectively desorption gasification black aquatic suspended solid, hardness, three types of materials of ammonia nitrogen to realize reducing device demineralized water quantity and waste water discharge, alleviate equipment pipeline deposition scale deposit, extension fixture operation cycle's purpose has saved the water resource simultaneously and has protected more the environment.
The utility model provides a concrete scheme is:
a gasified black water treatment device comprises a primary flash tank, a secondary flash tank, a tertiary flash tank, a settling tank, an ash water tank, an ammonia distillation tower and a hot water tower,
the water outlet of the first-stage flash tank is communicated with the second-stage flash tank, the water outlet of the second-stage flash tank is communicated with the third-stage flash tank,
the water outlet of the third-level flash tank is communicated with a settling tank, a pipeline mixer is connected between the water outlet of the third-level flash tank and the settling tank, a sectional dosing pipe is installed in the settling tank, the water outlet of the settling tank is communicated with an ash water tank, the water outlet of the ash water tank is communicated with an ammonia still, the water outlet of the ammonia still is communicated with a hot water tower, and the effluent of the hot water tower is conveyed to a crude synthesis gas washing section.
A steam outlet of a first-stage flash tank in the gasified black water treatment device is communicated with the lower part of a hot water tower, and a steam outlet at the top of the hot water tower is communicated with the lower part of an ammonia still.
The steam outlet of the secondary flash tank in the gasification black water treatment device is communicated with the lower part of the ammonia still.
The sectional chemical feeding pipe in the gasified black water treatment device is an annular chemical feeding pipe, a chemical feeding pipe opening is formed in the annular chemical feeding pipe, and chemical releasing holes are distributed at the bottom of the annular chemical feeding pipe.
The annular chemical feeding pipe in the gasification black water treatment device comprises an inner annular pipe and an outer annular pipe, the inner annular pipe and the outer annular pipe are communicated through a communicating pipe, and the bottom parts of the inner annular pipe and the outer annular pipe are provided with chemical releasing holes.
The inner ring pipe and the outer ring pipe in the gasification black water treatment device are communicated through communicating pipes which are uniformly distributed.
The gasified black water treatment device also comprises a grey water heater, the water outlet of the grey water tank is connected with the grey water heater, the grey water heater is connected with an ammonia gas outlet at the top of the ammonia still, and the water outlet of the grey water heater is communicated with the ammonia still.
The utility model discloses an useful part is:
the utility model provides a gasification black water treatment device, which utilizes a first-level flash tank and a second-level flash tankThe three-level flash tank carries out multi-level flash evaporation, and a pipeline mixer is arranged between the three-level flash tank and the settling tank so as to quantitatively add CO in advance2Fully mixing with flocculating agent, and adding alkali liquor in the settling tank by using sectional dosing pipes in a sectional manner to prevent CaCO from entering the settling tank3The crystal is separated out to cause the black water pipeline in the sedimentation tank to be scaled and blocked, and the coal ash particles in the black water are used as crystal nuclei to ensure that the supersaturated CaCO in the black water3Continuously adsorbing the coal ash particles to form crystals with larger particle size, being convenient for full sedimentation, simultaneously removing the hardness and suspended matters of black water, avoiding CaCO3Spontaneous nucleation at high degree of supersaturation to form superfine CaCO3The crystal reduces the settling effect of the settling tank, causes the problem of rising of suspended solids in the outlet water, and after settling, the ash water enters the ash water tank and then enters the ammonia still for ammonia stripping, and after the deamination is completed, the hot water tower can reach the crude synthesis gas washing working section again, the device can effectively remove three substances of suspended solids, hardness and ammonia nitrogen in the gasified black water, and realize the reduction of the desalted water consumption and the wastewater discharge amount of the device, relieve the dust deposition and scaling of the equipment pipeline, achieve the purpose of prolonging the operation period of the device, save water resources and protect environment;
drawings
FIG. 1 is a schematic view of the connection of the device of the present invention;
FIG. 2 is an enlarged top view of the sectional loading tube;
FIG. 3 is a schematic top view of the position of the sectional dosing tube in the settling tank.
Reference numerals:
the system comprises a primary flash tank 1, a secondary flash tank 2, a tertiary flash tank 3, a circulating water cooler 4, a first pipeline mixer 5, a settling tank 6, an annular chemical feeding pipe 7, an inner ring pipe 71, an outer ring pipe 72, a communicating pipe 73, a chemical inlet pipe opening 74, a vacuum pump 8, an ash water tank 9, a hot water tower 10, a low-pressure ash water pump 11, an ash water heater 12, an ammonia still 13, a second pipeline mixer 14, a medium-pressure ash water pump 15, a high-pressure ash water pump 16, a raking machine material rake 17 and a raking machine rotating shaft 18.
Detailed Description
The utility model provides a gasification black water treatment device, which comprises a primary flash tank, a secondary flash tank, a tertiary flash tank, a settling tank, an ash water tank, an ammonia distillation tower and a hot water tower,
the water outlet of the first-stage flash tank is communicated with the second-stage flash tank, the water outlet of the second-stage flash tank is communicated with the third-stage flash tank,
the water outlet of the third-level flash tank is communicated with a settling tank, a pipeline mixer is connected between the water outlet of the third-level flash tank and the settling tank, a sectional dosing pipe is installed in the settling tank, the water outlet of the settling tank is communicated with an ash water tank, the water outlet of the ash water tank is communicated with an ammonia still, the water outlet of the ammonia still is communicated with a hot water tower, and the effluent of the hot water tower is conveyed to a crude synthesis gas washing section.
The present invention is further described with reference to the following drawings and specific embodiments so that those skilled in the art can better understand the present invention and can implement the present invention, but the embodiments are not to be construed as limiting the present invention.
In one embodiment of the utility model, the system comprises a primary flash tank 1, a secondary flash tank 2, a tertiary flash tank 3, a first pipeline mixer 5, a settling tank 6, an ash water tank 9, a hot water tower 10,
the water outlet of the three-level flash tank 3 is communicated with a settling tank 6, a first pipeline mixer 5 is connected between the water outlet of the three-level flash tank 3 and the settling tank 6, an annular chemical feeding pipe 7 is installed in the settling tank 6, a chemical feeding pipe opening 74 is formed in the annular chemical feeding pipe 7, chemical releasing holes are distributed in the bottom of the annular chemical feeding pipe 7 and used for releasing added alkali liquor in a segmented mode, the water outlet of the settling tank 6 is communicated with an ash water tank 9, the water outlet of the ash water tank 9 is communicated with an ammonia still 13, the water outlet of the ammonia still 13 is communicated with a hot water tower 10, and effluent of the hot water tower 10 is conveyed to a.
In the embodiment, the primary flash tank, the secondary flash tank and the tertiary flash tank are used for multi-stage flash, the first pipeline mixer 5 is arranged between the tertiary flash tank 3 and the settling tank 6 so as to quantitatively add CO2 and the flocculating agent in advance and fully mix the CO2 and the flocculating agent, and then the annular chemical adding pipe is used for sectionally adding alkali liquor in the settling tank 6 so as to prevent CaCO from being arranged before entering the settling tank 63The crystal is separated out to cause the black water pipeline entering the settling tank 6 to be scaled and blocked, and the coal ash particles in the black water are used as crystal nuclei to ensure that the supersaturated CaCO in the black water3Continuously adsorb to coalCrystals with larger particle size are formed on the ash particles, so that the crystals can be conveniently and fully settled, the settled ash water enters an ash water tank 9 and then enters an ammonia still 13 for ammonia stripping, and after the ammonia stripping is finished, a hot water tower 10 can reach a crude synthesis gas washing section again.
On the basis of the above embodiment, the annular dosing pipe 7 comprises an inner annular pipe 71 and an outer annular pipe 72, the inner annular pipe 71 and the outer annular pipe 74 are communicated through a communication pipe 73, and the inner annular pipe 71 and the outer annular pipe 72 are distributed with drug releasing holes, so that alkali liquor is released in sections more uniformly, and the drug releasing holes can be distributed uniformly, a reference specification is provided, for example, the diameter of the inner annular pipe is 1.5m, the diameter of the outer annular pipe is 2m, the diameters of the inner annular pipe and the outer annular pipe are both 5cm, the diameter of the drug releasing holes is 1-2mm, and 30-50 drug releasing holes are provided per meter of pipe.
The black water can enter the settling tank 6 from a central water inlet of the settling tank 6, and radially flows to the overflow weir along the settling tank 6, and firstly passes through the inner ring pipe 71 and then passes through the outer ring pipe 72 in the flowing process, when the medicine is added, the medicine enters the inner ring pipe 71 through the medicine inlet pipe orifice 74, one part of the medicine enters the settling tank 6 through the medicine releasing holes on the inner ring pipe 71, the other part of the medicine enters the outer ring pipe 72 through the communicating pipe 73, and enters the settling tank 6 through the medicine releasing holes of the outer ring pipe 72, so that the segmented medicine adding purpose with more obvious effect is achieved.
The annular dosing pipe 7 can be made of acid corrosion resistant materials, such as PVC, PPR, 304 stainless steel and the like, so that online acid washing can be performed when the annular dosing pipe 7 is scaled. And a filter is preferably arranged on the medicine inlet pipeline, and the precision of the filter is more than 1 mm.
During installation, the annular dosing pipe 7 can be hung on a cover plate and a steel beam at the top of the settling tank 6 in a conventional manner, and is preferably installed concentrically with the rotating shaft 18 of the raking machine of the settling tank 6, referring to the relative positions of the rotating shaft 18 of the raking machine, the rake 17 of the raking machine and the annular dosing pipe 7 in fig. 3.
In addition, the sectional dosing tube can be in other shapes or styles, and only the purpose of sectional dosing can be achieved.
In another embodiment of the present invention, based on the above embodiment, for better utilizing the heat of the steam of the first-level flash tank, the steam outlet of the first-level flash tank 1 is connected to the lower part of the hot water tower 10, and the steam outlet of the top of the hot water tower 10 is connected to the lower part of the ammonia still 13. The steam flashed off from the first-stage flash tank 1 is sent to a hot water tower 10 to recover heat for grey water heat exchange after stripping, and the surplus steam is sent to an ammonia still 13 through the hot water tower 10 to be used as stripping steam.
In another embodiment, the steam outlet of the two-stage flash tank 2 is communicated with the lower part of the ammonia still 13 on the basis of the above embodiment. Namely, the steam generated by the recovery secondary flash tank 2 is sent to the ammonia still 13 to be used as stripping steam.
In a specific operation embodiment, the pressure of the primary flash tank 1 is 0.4-0.6MPa, the steam flashed out is sent to a hot water tower 10 through a steam outlet to recover heat, the black water out of the primary flash tank 1 enters the secondary flash tank 2, the pressure of the secondary flash tank 2 is 0.2-0.3MPa, the steam flashed out is sent to an ammonia still 13 through a steam outlet to be used as stripping steam, the black water out of the secondary flash tank enters the tertiary flash tank 3, the pressure of the tertiary flash tank 3 is-0.07 MPa to-0.05 MPa, the steam flashed out can be cooled through a circulating water cooler 4, the non-condensable gas is pumped to atmosphere by a vacuum pump 8 to be emptied, the black water after being flashed enters a central water inlet pipe of the radial flow settling tank 6, a first pipeline mixer 5 is arranged on a pipeline before the radial flow settling tank 6, and a certain amount of CO is added into the black water through the first pipeline mixer 5.2And a flocculating agent, wherein an annular chemical feeding pipe 7 is arranged in the radial flow settling tank 6, alkali liquor is added in sections through the annular chemical feeding pipe 7, the addition amount of the alkali liquor is determined according to the measurement value of a PH value at an outlet of the radial flow settling tank 6, the PH value of water discharged from the radial flow settling tank 6 is generally controlled to be 10-11, settled ash water enters an ash water tank 9, is pressurized by a low-pressure ash water pump 11, enters an ash water heater 12 to exchange heat with ammonia-rich gas discharged from the top of an ammonia still 13, then enters the ammonia still 13 to carry out ammonia stripping, the pressure of the ammonia still is controlled to be 0.15-0.25MPa, the temperature of a tower bottom is 130-135 ℃, the stripped ash water is added with sulfuric acid through a second pipeline mixer 14 to adjust the PH value to be 7-8, and then is conveyed to the first-stage flash evaporation steam drum 1 through a medium-pressure ash water pump 15 to.
CO2The amount of (c) can be calculated according to the following formula:
A＝(B-3)*Q*22.4
wherein A-CO2Flow rate, Nm3H, B-hardness of black water entering the settler, mmol/L, Q-flow of black water entering the settler, m3/h；
Ammonia stripping is carried out on settled ash water, the PH is increased by using alkali liquor added in the process of hardness removal, and NH in the ash water is promoted by higher PH3·H2O═NH4 ++OH-The ionization balance moves towards the reverse direction, which is more beneficial to ammonia stripping operation and reduces the ammonia nitrogen content of the grey water;
and (4) transferring the stripped grey water to a raw synthesis gas washing section after heat exchange.
The alkali liquor mentioned in the operation of the utility model is preferably NaOH, Ca (OH)2Strong alkali such as KOH and the like, NaOH is most preferable from the viewpoint of cost.
The above-mentioned embodiments are merely preferred embodiments for fully illustrating the present invention, and the scope of the present invention is not limited thereto. Equivalent substitutes or changes made by the technical personnel in the technical field on the basis of the utility model are all within the protection scope of the utility model. The protection scope of the present invention is subject to the claims.
Claims (10)
1. A gasified black water treatment device is characterized by comprising a primary flash tank, a secondary flash tank, a tertiary flash tank, a settling tank, an ash water tank, an ammonia distillation tower and a hot water tower,
the water outlet of the first-stage flash tank is communicated with the second-stage flash tank, the water outlet of the second-stage flash tank is communicated with the third-stage flash tank,
the water outlet of the third-level flash tank is communicated with a settling tank, a pipeline mixer is connected between the water outlet of the third-level flash tank and the settling tank, a sectional dosing pipe is installed in the settling tank, the water outlet of the settling tank is communicated with an ash water tank, the water outlet of the ash water tank is communicated with an ammonia still, the water outlet of the ammonia still is communicated with a hot water tower, and the effluent of the hot water tower is conveyed to a crude synthesis gas washing section.
2. The gasification black water treatment device of claim 1, wherein the steam outlet of the first-stage flash tank is connected to the lower part of the hot water tower, and the steam outlet at the top of the hot water tower is connected to the lower part of the ammonia still.
3. The gasification black water treatment device according to claim 1 or 2, wherein the steam outlet of the secondary flash tank is communicated with the lower part of the ammonia still.
4. The gasification black water treatment device according to claim 1, wherein the segmented chemical feeding pipe is an annular chemical feeding pipe, the annular chemical feeding pipe is provided with a chemical feeding pipe opening, and the bottom of the annular chemical feeding pipe is provided with chemical release holes.
5. The gasification black water treatment device according to claim 3, wherein the segmented chemical feeding pipe is an annular chemical feeding pipe, the annular chemical feeding pipe is provided with a chemical feeding pipe opening, and the bottom of the annular chemical feeding pipe is provided with chemical release holes.
6. The black water treatment device for gasification according to claim 4, wherein the annular chemical feeding pipe comprises an inner annular pipe and an outer annular pipe, the inner annular pipe and the outer annular pipe are communicated through a communicating pipe, and the bottom parts of the inner annular pipe and the outer annular pipe are provided with chemical releasing holes.
7. The black water treatment device for gasification according to claim 5, wherein the annular chemical feeding pipe comprises an inner annular pipe and an outer annular pipe, the inner annular pipe and the outer annular pipe are communicated through a communicating pipe, and the bottom parts of the inner annular pipe and the outer annular pipe are provided with chemical releasing holes.
8. The black water treatment device for gasification according to claim 6 or 7, wherein the inner annular pipe and the outer annular pipe are communicated by evenly distributed communicating pipes.
9. The gasified black water treatment device according to claim 1, 6 or 7, further comprising a grey water heater, wherein the water outlet of the grey water tank is connected with the grey water heater, the grey water heater is connected with an ammonia gas outlet at the top of the ammonia distillation tower, and the water outlet of the grey water heater is communicated with the ammonia distillation tower.
10. The gasified black water treatment device of claim 8, further comprising a grey water heater, wherein the outlet of the grey water tank is connected with the grey water heater, the grey water heater is connected with an ammonia gas outlet at the top of the ammonia still tower, and the outlet of the grey water heater is communicated with the ammonia still tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020965771.5U CN212741038U (en) | 2020-06-01 | 2020-06-01 | Gasification black water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020965771.5U CN212741038U (en) | 2020-06-01 | 2020-06-01 | Gasification black water treatment device |
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| CN212741038U true CN212741038U (en) | 2021-03-19 |
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| CN202020965771.5U Active CN212741038U (en) | 2020-06-01 | 2020-06-01 | Gasification black water treatment device |
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