CN208414630U - The cooling water recirculation system of silicon material ingot casting boiler - Google Patents
The cooling water recirculation system of silicon material ingot casting boiler Download PDFInfo
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- CN208414630U CN208414630U CN201820957595.3U CN201820957595U CN208414630U CN 208414630 U CN208414630 U CN 208414630U CN 201820957595 U CN201820957595 U CN 201820957595U CN 208414630 U CN208414630 U CN 208414630U
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Abstract
The utility model discloses a kind of cooling water recirculation systems of silicon material ingot casting boiler, including the liquid argon tank to boiler supply argon gas, it is connected between liquid argon tank and boiler by vapourizing unit, boiler is equipped with boiler coolant liquid interlayer, the liquid feeding end A of the boiler coolant liquid interlayer of boiler is connected to by pump housing A with the outlet end E of coolant reservoirs, the outlet end A of the boiler coolant liquid interlayer of boiler is connected to by heat-exchangers of the plate type with the liquid feeding end E of coolant reservoirs, vapourizing unit is equipped with heat exchanging interlayer A, and the heat exchanger coolant liquid of heat-exchangers of the plate type is connected to heat exchanging interlayer A.Known to from the above, the cooling water recirculation system of the silicon material ingot casting boiler of the utility model, make the heat exchange coolant liquid to boiler coolant liquid using the liquid argon vaporization heat absorption in the production technology of silicon material ingot casting boiler to freeze, while guaranteeing heat exchange effect, moreover it is possible to the vapourizing unit surface of liquid argon be made to avoid freezing.
Description
Technical field
The utility model relates to the technical fields of the cooling cycle of silicon material ingot casting boiler, and in particular to a kind of silicon material ingot casting pot
The cooling water recirculation system of furnace.
Background technique
In photoelectric field, silicon is extremely important and common raw semiconductor, is the optimal raw material of solar battery.
The process for preparing silicon wafer generally comprises the processes such as the cleaning of silicon raw material, silicon material ingot casting, silicon ingot butt, silicon side's slice.Entirely making
During standby, the maximum process of time-consuming longest, energy consumption is silicon material ingot casting.Silicon material after cleaning is put into boiler, in inert gas
Atmosphere under dissolve by heating, then crystallization form silicon ingot.During this, extreme temperatures in the crucible of ingot casting, in order to anti-
Only boiler is burnt out, and boiler is equipped with interlayer, is cooled down using coolant liquid to boiler itself.And cooling down the coolant liquid after boiler just needs
To cool down in time and be recycled to boiler herein and continue to cool down to boiler.Current enterprise is typically produced by refrigeration machine cold
But agent is to carrying out heat exchange cooling to the boiler coolant liquid after boiler cooling, but in this way will obviously be additional increase energy
Consumption.
In addition, argon gas is typically all to carry out transport storage with liquid argon state, it must but required when entering in boiler
It must be argon gas, and since liquid argon vaporization can absorb a large amount of heat, freeze to will lead to hydraulic vapourizing unit, not only influences
The efficiency for continuing vaporization of liquid argon, nor safeguarded convenient for the dismounting to gasification installation；And it is vaporized by vapourizing unit
Temperature of argon gas afterwards is very low with respect to for the temperature in boiler, so will lead in boiler after argon gas enters in boiler
Temperature generates fluctuation, not only further increases the energy consumption of boiler ingot casting, but also will affect the quality of silicon material ingot casting.
Summary of the invention
The purpose of this utility model is that: overcome the deficiencies of the prior art and provide a kind of cooling water of silicon material ingot casting boiler
The circulatory system is absorbed heat cold to the heat exchange of boiler coolant liquid to make using the liquid argon vaporization in the production technology of silicon material ingot casting boiler
But liquid freezes, and while guaranteeing heat exchange effect, reduces production energy consumption, and can also make the vapourizing unit surface of liquid argon
It avoids freezing, and then is safeguarded convenient for the dismounting of vapourizing unit；Passed through using the boiler coolant liquid after cooling boiler to vaporization
Argon gas afterwards is preheated before entering boiler, so that the lower argon gas of temperature be avoided to enter after boiler to the temperature in boiler
Cause to fluctuate, to influence the quality of silicon material ingot casting and increase energy consumption, while preheat argon gas while is also to boiler coolant liquid
Primary pre-cooling is carried out, to can also make boiler coolant liquid that can fast and effeciently cool down after cooling boiler, to follow
Boiler is cooled down again after ring；Argon gas is avoided so that the heat exchange effect of vapourizing unit improves by the effect of gathering tube
In the larger situation of usage amount, vapourizing unit still is able to normal use, and freezeout will not occur；By the effect of cooling tower,
To when the heating power when boiler is higher, pot in-furnace temperature is higher, it is ensured that boiler coolant liquid is gone back after circulation
Boiler can be carried out effectively cooling.
Technical solution adopted in the utility model is:
The cooling water recirculation system of silicon material ingot casting boiler, the boiler including silicon material ingot casting further include supplying argon gas to boiler
Liquid argon tank, between the liquid argon tank and boiler by vapourizing unit connect, the boiler be equipped with boiler coolant liquid interlayer, it is described
The liquid feeding end A of the boiler coolant liquid interlayer of boiler is connected to by pump housing A with the outlet end E of coolant reservoirs, the boiler of the boiler
The outlet end A of coolant liquid interlayer is connected to by heat-exchangers of the plate type with the liquid feeding end E of coolant reservoirs, and the vapourizing unit is equipped with
The outlet end C of heat exchanging interlayer A, the liquid feeding end B and heat exchanging interlayer A of the heat exchanger coolant liquid of the heat-exchangers of the plate type are connected to,
The liquid feeding end C of the outlet end B and heat exchanging interlayer A of the heat exchanger coolant liquid of the heat-exchangers of the plate type are connected to.
The utility model is further improved scheme, and the vapourizing unit is connected to liquid argon tank by liquid argon delivery pipe, is logical
It crosses argon delivery lines to be connected to boiler, the surface of the argon delivery lines is equipped with heat exchanging interlayer B, the feed liquor of the heat exchanging interlayer B
End D is connected to by pipeline A with the outlet end A of boiler cooling sandwith layer, the outlet end D of the heat exchanging interlayer B pass through pipeline B with it is board-like
The boiler coolant liquid liquid feeding end of heat exchanger is connected to.
The further improvement project of the utility model is the outlet end of the heat exchanger coolant liquid of the heat-exchangers of the plate type
B is connected to by pipeline C with the outlet end C of heat exchanging interlayer A, the pipeline C by tee tube A respectively parallel communication have pipeline D with
Pipeline E, the pipeline D and pipeline E pass through tee tube C respectively and are connected to pipeline F, and go out liquid by pipeline F and heat exchanging interlayer A
Hold C connection.
The further improvement project of the utility model is that the pipeline F is equipped with pump housing B.
The further improvement project of the utility model is that the boiler coolant liquid outlet end of the heat-exchangers of the plate type is communicated with
Pipeline G, the pipeline D are directly connected to pipeline F, the pipeline E is connected to pipeline G by tee tube B to form gathering tube after, then
It is connected to by tee tube C with pipeline F, the gathering tube is equipped with tee tube D, and the gathering tube is connected by tee tube D and pipeline H
It is logical, and be connected to by pipeline H with the liquid feeding end E of coolant reservoirs.
The further improvement project of the utility model is that the pipeline D is equipped with valve A, and the pipeline E is equipped with valve
B is additionally provided with valve C between the tee tube C and tee tube D.
The further improvement project of the utility model is that the pipeline H is connected to by tee tube E with pipeline I, the pipeline
I is connected to the liquid feeding end F of cooling tower, and the outlet end F of the cooling tower is connected to by pipeline J with the liquid feeding end E ' of coolant reservoirs.
The further improvement project of the utility model is, the pipeline I is equipped with valve D, and the pipeline H is upper, positioned at three
Valve E is equipped between siphunculus E and coolant reservoirs.
The further improvement project of the utility model is that the liquid feeding end A of the boiler coolant liquid interlayer of the boiler passes through pipe
Road K is connected to the outlet end E of coolant reservoirs, and the pump housing A is communicated on pipeline K.
The further improvement project of the utility model is that the outlet end C of the heat exchanging interlayer A passes through pipeline L and board-like heat
The liquid feeding end B of the heat exchanger coolant liquid of exchanger is connected to.
The utility model has the beneficial effects that:
The first, the cooling water recirculation system of the silicon material ingot casting boiler of the utility model, utilizes the production of silicon material ingot casting boiler
Liquid argon vaporization heat absorption in technique is freezed come the heat exchange coolant liquid for making to boiler coolant liquid, guarantees the same of heat exchange effect
When, production energy consumption is reduced, and the vapourizing unit surface of liquid argon can also be made to avoid freezing, and then be convenient for the dismounting of vapourizing unit
Maintenance.
The second, the cooling water recirculation system of the silicon material ingot casting boiler of the utility model utilizes the pot after cooling boiler
Furnace coolant liquid before entering boiler by preheating the argon gas after vaporization, so that the lower argon gas of temperature be avoided to enter pot
The temperature in boiler is caused to fluctuate after furnace, to influence the quality of silicon material ingot casting and increase energy consumption, while preheating the same of argon gas
When be also that primary pre-cooling has been carried out to boiler coolant liquid, to can also make boiler coolant liquid can be quick after cooling boiler
Effectively cool down, to be cooled down again to boiler after circulation.
Third, the utility model silicon material ingot casting boiler cooling water recirculation system, by the effect of gathering tube, so that vapour
Disguise the heat exchange effect set to improve, avoid in the larger situation of argon gas usage amount, vapourizing unit still is able to normal use, will not
Freezeout occurs.
4th, the cooling water recirculation system of the silicon material ingot casting boiler of the utility model, by the effect of cooling tower, to work as
When the heating power of boiler is higher, pot in-furnace temperature is higher, it is ensured that boiler coolant liquid can also be right after circulation
Boiler carries out effectively cooling.
Detailed description of the invention:
Fig. 1 is the schematic diagram of the utility model structure.
Specific embodiment:
As shown in Figure 1, the cooling water recirculation system of the silicon material ingot casting boiler of the utility model includes the boiler of silicon material ingot casting
1, further include the liquid argon tank 2 for supplying argon gas to boiler 1, is connected between the liquid argon tank 2 and boiler 1 by vapourizing unit 3, it is described
Boiler 1 is equipped with boiler coolant liquid interlayer, and the liquid feeding end A of the boiler coolant liquid interlayer of the boiler 1 passes through pump housing A24 and coolant liquid
The outlet end E in pond 9 is connected to, and the outlet end A of the boiler coolant liquid interlayer of the boiler 1 passes through heat-exchangers of the plate type 8 and coolant liquid
The liquid feeding end E in pond 9 is connected to, and the vapourizing unit 3 is equipped with heat exchanging interlayer A6, and the heat exchanger of the heat-exchangers of the plate type 8 is cold
But the outlet end C of the liquid feeding end B and heat exchanging interlayer A6 of liquid are connected to, and the heat exchanger coolant liquid of the heat-exchangers of the plate type 8 goes out
Liquid end B is connected to the liquid feeding end C of heat exchanging interlayer A6；The vapourizing unit 3 is connected to liquid argon tank 2, is passed through by liquid argon delivery pipe 4
Argon delivery lines 5 are connected to boiler 1, and the surfaces of the argon delivery lines 5 is equipped with heat exchanging interlayer B7, the heat exchanging interlayer B7 into
Liquid end D is connected to by pipeline A12 with the outlet end A of boiler cooling sandwith layer, and the outlet end D of the heat exchanging interlayer B7 passes through pipeline
B13 is connected to the boiler coolant liquid liquid feeding end of heat-exchangers of the plate type 8；The heat exchanger coolant liquid of the heat-exchangers of the plate type 8
Outlet end B is connected to by pipeline C17 with the outlet end C of heat exchanging interlayer A6, and the pipeline C17 connects by the way that tee tube A is in parallel respectively
It is connected with pipeline D21 and pipeline E22, the pipeline D21 and pipeline E22 passes through tee tube C respectively and be connected to pipeline F15, and pass through
Pipeline F15 is connected to the outlet end C of heat exchanging interlayer A6；The pipeline F15 is equipped with pump housing B25；The pot of the heat-exchangers of the plate type 8
Furnace coolant liquid outlet end is communicated with pipeline G14, and the pipeline D21 is directly connected to pipeline F15, the pipeline E22 and pipeline G14
It is connected to by tee tube B after forming gathering tube 23, then is connected to by tee tube C with pipeline F15, the gathering tube 23 is equipped with three
Siphunculus D, the gathering tube 23 are connected to by tee tube D with pipeline H18, and pass through the liquid feeding end E of pipeline H18 and coolant reservoirs 9
Connection；The pipeline D21 be equipped with valve A27, the pipeline E22 be equipped with valve B28, the tee tube C and tee tube D it
Between be additionally provided with valve C29；The pipeline H18 is connected to by tee tube E with pipeline I19, the pipeline I19 and cooling tower 10 into
The outlet end F of liquid end F connection, the cooling tower 10 is connected to by pipeline J20 with the liquid feeding end E ' of coolant reservoirs 9；The pipeline
I19 is equipped with valve D26, the pipeline H18 is upper, between tee tube E and coolant reservoirs 9 equipped with valve E30；The boiler
The liquid feeding end A of 1 boiler coolant liquid interlayer is connected to by pipeline K11 with the outlet end E of coolant reservoirs 9, the pump housing A24 connection
On pipeline K11；The outlet end C of the heat exchanging interlayer A6 is cooling by the heat exchanger of pipeline L16 and heat-exchangers of the plate type 8
The liquid feeding end B of liquid is connected to.The boiler coolant liquid is water, the coolant liquid in the coolant reservoirs 9 is water, the board-like heat exchange
The heat exchanger coolant liquid of device 8 is also water.
When the utility model normal use, the water in coolant reservoirs 9 is delivered to the boiler of boiler 1 by pump housing A24
The liquid feeding end A of coolant liquid interlayer, cools down boiler 1, when boiler 1 begins to use, due in boiler 1 temperature compared with
Height makes the temperature of the water of the outlet end A of boiler coolant liquid interlayer so the water in boiler coolant liquid interlayer cools down boiler
It is higher, when then boiler uses, since reaction is needed using argon gas as protection gas, so the liquid argon in liquid argon tank 2 needs
It is vaporized by vapourizing unit 3, and the process vaporized needs to absorb heat, so can be to playing cooling work around vapourizing unit 3
With, and the temperature of argon gas in the argon delivery lines 5 after vaporizing is relatively low, being directly entered in boiler 1 can be to the temperature in boiler 1
It has an impact, causes the silicon material ingot casting time to extend, energy consumption increases；So the heat exchanger coolant liquid feed liquor of heat-exchangers of the plate type 8
After end is connected to the outlet end C of heat exchanging interlayer A6 set by vapourizing unit 3, the water temperature of heat exchanger coolant liquid liquid feeding end is extremely low,
And the heat exchanging interlayer B7 of argon delivery lines 5 is exchanged heat by just carrying out the higher water of cooling temperature to boiler 1, to make argon
Argon gas in letter shoot 5 is preheated, while the argon gas in argon delivery lines 5 to boiler 1 also to just carrying out cooling temperature
Higher water is cooled down for the first time；Then board-like heat is again passed by by the water that the argon gas in argon delivery lines 5 cools down for the first time to hand over
Parallel operation 8, the water progressive heat exchange cooling with vapourizing unit 3 is passed through, to cool down again；Valve A27 and valve E30 is opened,
Valve B28 and valve C29 is closed, and then the water of the heat exchanger coolant liquid Jing Guo heat exchange is again introduced into changing for vapourizing unit 3
Hot interlayer A6 carries out cooling refrigeration, and the water of the boiler coolant liquid by heat exchange then enters coolant reservoirs 9.
When argon gas usage amount is larger, valve A27 is closed, and valve B28, valve C29 and valve E30 are opened, thus
The flow for increasing the water in the heat exchanging interlayer A6 of vapourizing unit 3 avoids vapourizing unit 3 from freezing, while also can be further
Improve the cooling effect of boiler coolant liquid.
The power consumption needed for silicon material ingot casting in boiler 1 is larger, cause temperature is higher, when need cooling amount larger,
Since the specific discharge of the boiler coolant liquid in the boiler coolant liquid interlayer of boiler 1 will not change, so leading to boiler coolant liquid
The temperature of the water of the outlet end A of interlayer can be higher, and after heat-exchangers of the plate type 8, the boiler of heat-exchangers of the plate type 8 is cold
But the temperature of the water of liquid outlet end still can be higher, and valve D26 is opened at this time, and valve E30 is closed, and makes heat-exchangers of the plate type 8
The water of boiler coolant liquid outlet end can first pass through after cooling tower 10 further cools down and enter back into coolant reservoirs 9, guarantee pump housing A24
The water temperature being delivered in boiler coolant liquid interlayer from coolant reservoirs 9 can achieve the effect that effective temperature-reducing boiler 1.
Claims (10)
1. the cooling water recirculation system of silicon material ingot casting boiler, it is characterised in that: the boiler (1) including silicon material ingot casting, further include to
Boiler (1) supplies the liquid argon tank (2) of argon gas, is connect between the liquid argon tank (2) and boiler (1) by vapourizing unit (3), described
Boiler (1) is equipped with boiler coolant liquid interlayer, and the liquid feeding end A of the boiler coolant liquid interlayer of the boiler (1) passes through pump housing A(24) with
The outlet end E of coolant reservoirs (9) is connected to, and the outlet end A of the boiler coolant liquid interlayer of the boiler (1) passes through heat-exchangers of the plate type
(8) it is connected to the liquid feeding end E of coolant reservoirs (9), the vapourizing unit (3) is equipped with heat exchanging interlayer A(6), the board-like heat is handed over
The outlet end C of the liquid feeding end B and heat exchanging interlayer A(6) of the heat exchanger coolant liquid of parallel operation (8) are connected to, the heat-exchangers of the plate type
(8) the liquid feeding end C of the outlet end B and heat exchanging interlayer A(6) of heat exchanger coolant liquid are connected to.
2. the cooling water recirculation system of silicon material ingot casting boiler as described in claim 1, it is characterised in that: the vapourizing unit
(3) it is connected to by liquid argon delivery pipe (4) with liquid argon tank (2), is connected to by argon delivery lines (5) with boiler (1), the argon gas is defeated
Send pipe (5) surface be equipped with heat exchanging interlayer B(7), the heat exchanging interlayer B(7) liquid feeding end D pass through pipeline A(12) it is cold with boiler
But the outlet end A connection of interlayer, the heat exchanging interlayer B(7) outlet end D pass through pipeline B(13) with heat-exchangers of the plate type (8)
The connection of boiler coolant liquid liquid feeding end.
3. the cooling water recirculation system of silicon material ingot casting boiler as described in claim 1, it is characterised in that: the board-like heat exchange
The outlet end B of the heat exchanger coolant liquid of device (8) passes through pipeline C(17) it is connected to the outlet end C of heat exchanging interlayer A(6), the pipe
Road C(17) by tee tube A, parallel communication has pipeline D(21 respectively) and pipeline E(22), the pipeline D(21) and pipeline E(22)
It is connected to respectively by tee tube C with pipeline F(15), and passes through pipeline F(15) it is connected to the outlet end C of heat exchanging interlayer A(6).
4. the cooling water recirculation system of silicon material ingot casting boiler as claimed in claim 3, it is characterised in that: the pipeline F(15)
Equipped with pump housing B(25).
5. the cooling water recirculation system of silicon material ingot casting boiler as claimed in claim 3, it is characterised in that: the board-like heat exchange
The boiler coolant liquid outlet end of device (8) is communicated with pipeline G(14), the pipeline D(21) directly it is connected to pipeline F(15), it is described
Pipeline E(22) be connected to pipeline G(14) by tee tube B and to form gathering tube (23) after, then pass through tee tube C and pipeline F(15)
Connection, the gathering tube (23) are equipped with tee tube D, and the gathering tube (23) is connected to by tee tube D with pipeline H(18), and
It is connected to by pipeline H(18) with the liquid feeding end E of coolant reservoirs (9).
6. the cooling water recirculation system of silicon material ingot casting boiler as claimed in claim 5, it is characterised in that: the pipeline D(21)
It is equipped with valve A(27), the pipeline E(22) it is equipped with valve B(28), valve is additionally provided between the tee tube C and tee tube D
Door C(29).
7. the cooling water recirculation system of silicon material ingot casting boiler as claimed in claim 5, it is characterised in that: the pipeline H(18)
It is connected to by tee tube E with pipeline I(19), the pipeline I(19) it is connected to the liquid feeding end F of cooling tower (10), the cooling tower
(10) outlet end (F) passes through pipeline J(20) it is connected to the liquid feeding end E ' of coolant reservoirs (9).
8. the cooling water recirculation system of silicon material ingot casting boiler as claimed in claim 7, it is characterised in that: the pipeline I(19)
Be equipped with valve D(26), the pipeline H(18) on, positioned at tee tube E and coolant reservoirs (9) between equipped with valve E(30).
9. the cooling water recirculation system of silicon material ingot casting boiler as described in claim 1, it is characterised in that: the boiler (1)
The liquid feeding end A of boiler coolant liquid interlayer passes through pipeline K(11) be connected to the outlet end E of coolant reservoirs (9), the pump housing A(24)
It is communicated in pipeline K(11) on.
10. the cooling water recirculation system of silicon material ingot casting boiler as described in claim 1, it is characterised in that: the heat exchanging interlayer A
(6) outlet end C passes through pipeline L(16) it is connected to the liquid feeding end B of the heat exchanger coolant liquid of heat-exchangers of the plate type (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820957595.3U CN208414630U (en) | 2018-06-21 | 2018-06-21 | The cooling water recirculation system of silicon material ingot casting boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820957595.3U CN208414630U (en) | 2018-06-21 | 2018-06-21 | The cooling water recirculation system of silicon material ingot casting boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208414630U true CN208414630U (en) | 2019-01-22 |
Family
ID=65109124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820957595.3U Expired - Fee Related CN208414630U (en) | 2018-06-21 | 2018-06-21 | The cooling water recirculation system of silicon material ingot casting boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208414630U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108441947A (en) * | 2018-06-21 | 2018-08-24 | 江苏迩高新能源科技有限公司 | The cooling water recirculation system of silicon material ingot casting boiler |
-
2018
- 2018-06-21 CN CN201820957595.3U patent/CN208414630U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108441947A (en) * | 2018-06-21 | 2018-08-24 | 江苏迩高新能源科技有限公司 | The cooling water recirculation system of silicon material ingot casting boiler |
| CN108441947B (en) * | 2018-06-21 | 2024-01-02 | 江苏迩高新能源科技有限公司 | Cooling water circulation system of silicon ingot casting boiler |
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Granted publication date: 20190122 Termination date: 20190621 |
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| CF01 | Termination of patent right due to non-payment of annual fee |