CN218642800U - High-temperature high-pressure desorption electrolysis system heater pipeline device - Google Patents
High-temperature high-pressure desorption electrolysis system heater pipeline device Download PDFInfo
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- CN218642800U CN218642800U CN202222321615.7U CN202222321615U CN218642800U CN 218642800 U CN218642800 U CN 218642800U CN 202222321615 U CN202222321615 U CN 202222321615U CN 218642800 U CN218642800 U CN 218642800U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
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Abstract
The utility model provides a high temperature high pressure desorption electrolysis system heater pipe-line set, includes the desorption post, the desorption post passes through the pipeline and is connected with the filter, the filter passes through the pipeline and is connected with the electrolysis trough, the electrolysis trough is connected with the compensating tank, the compensating tank is connected with the ball valve, the ball valve respectively with join in marriage cistern and magnetic force actuation pump, magnetic force actuation pump is connected with electric heater, electric heater passes through the pipeline and is connected with desorption post and condenser respectively, the condenser is connected with joining in marriage the cistern. The utility model discloses a mode of "establishing ties alone", "parallelly connected alone" or "series-parallel" is connected, it is fast to make it both have electric heater "establish ties" intensification, the thermal efficiency is high, power consumptive few, running cost low grade advantage, it can avoid effectively stopping just can handle its drawback to have "parallelly connected" when electric heater breaks down again, when the guarantee normal gold carbon desorption electrolysis production of carrying, reduce the energy consumption that handles the electric heating trouble and the waste of cost.
Description
Technical Field
The utility model relates to a desorption electrolysis equipment technical field, concretely relates to high temperature high pressure desorption electrolysis system heater piping installation.
Background
The desorption electrolysis system is one of the commonly used processes in the gold industry, the heating efficiency of an electric heater of the existing desorption electrolysis system is not high, high-temperature and high-pressure desorption electrolysis is mostly adopted for accelerating the desorption speed, but the efficiency is not high due to the low heating efficiency of the electric heater, the time required by secondary production is longer after the system is stopped and cooled, and the like.
Disclosure of Invention
To the technical problem, the utility model provides a high temperature high pressure desorption electrolysis system heater piping installation, concrete technical scheme is:
the utility model provides a high temperature high pressure desorption electrolysis system heater pipe-line set, includes the desorption post, the desorption post passes through the pipeline and is connected with the filter, the filter passes through the pipeline and is connected with the electrolysis trough, the electrolysis trough is connected with the compensating tank, the compensating tank is connected with the ball valve, the ball valve respectively with join in marriage cistern and magnetic force actuation pump, magnetic force actuation pump is connected with electric heater, electric heater passes through the pipeline and is connected with desorption post and condenser respectively, the condenser is connected with joining in marriage the cistern.
Preferably, the electric heaters are provided in three.
Preferably, the three electric heaters are connected in sequence.
Preferably, the magnetic force drive pump is connected with a first ball valve a, the first ball valve a is respectively connected with a second ball valve a and a fourth ball valve a through pipelines, the second ball valve a is respectively connected with a third ball valve a and a sixth ball valve a through pipelines, the fourth ball valve a is connected with a fifth ball valve a, the sixth ball valve a is connected with a seventh ball valve a, the third ball valve a is connected with an eighth ball valve a, and the eighth ball valve a and the seventh ball valve a are both connected with a ninth ball valve a;
electric heaters are arranged between the fourth ball valve a and the fifth ball valve a, between the sixth ball valve a and the seventh ball valve a, and between the third ball valve a and the eighth ball valve a.
Preferably, the magnetic force drive pump is connected with a first ball valve b, the first ball valve b is respectively connected with a second ball valve b and a third ball valve b, the second ball valve b is respectively connected with a fourth ball valve b, a seventh ball valve b and a tenth ball valve b, the third ball valve b is connected with a fifth ball valve b, the fifth ball valve b is respectively connected with a fourth ball valve b and a sixth ball valve b, the sixth ball valve b is connected with an eighth ball valve b, the eighth ball valve b is respectively connected with a seventh ball valve b and a ninth ball valve b, the ninth ball valve b is connected with an eleventh ball valve b, and the eleventh ball valve b is respectively connected with a tenth ball valve b and a twelfth ball valve b;
and electric heaters are arranged between the third ball valve b and the fifth ball valve b, between the sixth ball valve b and the eighth ball valve b, and between the ninth ball valve b and the eleventh ball valve b.
The utility model discloses to carry electric heater pipeline among the gold charcoal high temperature high pressure integral pressure desorption electrolysis system and can adopt "establish ties alone", "parallelly connected" alone or the mode of "cluster and series-parallel connection" to connect, it is fast to make it both have electric heater "establish ties" intensification, the thermal efficiency is high, power consumptive few, running cost low grade advantage, it goes wrong can avoid effectively must stopping just can handle its drawback when electric heater breaks down to have "parallelly connected" again, when guarantee normal gold charcoal desorption electrolysis production that carries, reduce the energy consumption and the waste of cost of handling electric heating trouble and bringing.
Drawings
FIG. 1 is a schematic structural view of embodiment 1 of the present invention;
fig. 2 is a schematic structural view of embodiment 2 of the present invention;
fig. 3 is a schematic structural view of embodiment 3 of the present invention;
in the figure, 1-desorption column, 2-filter, 3-liquid preparation tank, 4-condenser, 5-electrolytic tank, 6-balance tank, 7-ball valve, 8-magnetic force drive pump and 9-electric heater;
901 a-ball valve a,902 a-ball valve a,903 a-ball valve a,904 a-ball valve a,905 a-ball valve a,906 a-ball valve a.907 a-ball valve a No. seven, 908 a-ball valve a No. eight, 909 a-ball valve a No. nine;
901 b-ball valve b,902 b-ball valve b,903 b-ball valve b,904 b-ball valve b,905 b-ball valve b,906 b-ball valve b.907 b-seven ball valve b,908 b-eight ball valve b,909 b-nine ball valve b,910 b-ten ball valve b,911 b-eleven ball valve b and 912 b-twelve ball valve b.
Detailed Description
For the purpose of better illustrating the embodiments, certain features of the drawings may be omitted, enlarged or reduced, and do not represent the size of an actual product; it will be understood by those skilled in the art that certain well-known structures in the drawings and descriptions thereof may be omitted. The specific meaning of the above terms in the present invention can be understood in specific cases for those skilled in the art. The technical solution of the present invention will be further explained with reference to the accompanying drawings and examples.
Example 1:
as shown in fig. 1, a high-temperature and high-pressure desorption electrolysis system heater pipeline device comprises a desorption column 1, wherein the desorption column 1 is connected with a filter 2 through a pipeline, the filter 2 is connected with an electrolysis bath 5 through a pipeline, the electrolysis bath 5 is connected with a balance tank 6, the balance tank 6 is connected with a ball valve 7, the ball valve 7 is respectively connected with a liquid distribution tank 3 and a magnetic force driving pump 8, the magnetic force driving pump 8 is connected with an electric heater 9, the electric heater 9 is respectively connected with the desorption column 1 and a condenser 4 through a pipeline, and the condenser 4 is connected with the liquid distribution tank 3.
In the present embodiment, three electric heaters 9 are provided. The three electric heaters 9 are connected in sequence.
In this embodiment, the electric heaters 9 are connected in series, and the heating efficiency is effectively improved by sequentially heating the three electric heaters 9.
Example 2:
as shown in fig. 2, a high-temperature and high-pressure desorption electrolysis system heater pipeline device comprises a desorption column 1, wherein the desorption column 1 is connected with a filter 2 through a pipeline, the filter 2 is connected with an electrolysis bath 5 through a pipeline, the electrolysis bath 5 is connected with a balance tank 6, the balance tank 6 is connected with a ball valve 7, the ball valve 7 is respectively connected with a liquid distribution tank 3 and a magnetic force driving pump 8, the magnetic force driving pump 8 is connected with an electric heater 9, the electric heater 9 is respectively connected with the desorption column 1 and a condenser 4 through a pipeline, and the condenser 4 is connected with the liquid distribution tank 3.
In the present embodiment, three electric heaters 9 are provided.
The magnetic force drive pump 8 is connected with a first ball valve a901a, the first ball valve a901a is respectively connected with a second ball valve a902a and a fourth ball valve a904a through pipelines, the second ball valve a902a is respectively connected with a third ball valve a903a and a sixth ball valve a906a through pipelines, the fourth ball valve a904a is connected with a fifth ball valve a905a, the sixth ball valve a906a is connected with a seventh ball valve a907a, the third ball valve a903a is connected with an eighth ball valve a908a, and the eighth ball valve a908a and the seventh ball valve a907a are both connected with a ninth ball valve a909 a;
In this embodiment, the electric heaters 9 are connected in parallel, and when one of the electric heaters 9 fails, the ball valves at both ends are closed to perform maintenance without affecting the operation of the system.
Example 3:
as shown in fig. 3, a high-temperature and high-pressure desorption electrolysis system heater pipeline device comprises a desorption column 1, wherein the desorption column 1 is connected with a filter 2 through a pipeline, the filter 2 is connected with an electrolysis bath 5 through a pipeline, the electrolysis bath 5 is connected with a balance tank 6, the balance tank 6 is connected with a ball valve 7, the ball valve 7 is respectively connected with a liquid distribution tank 3 and a magnetic force driving pump 8, the magnetic force driving pump 8 is connected with an electric heater 9, the electric heater 9 is respectively connected with the desorption column 1 and a condenser 4 through a pipeline, and the condenser 4 is connected with the liquid distribution tank 3.
In the present embodiment, three electric heaters 9 are provided.
The magnetic force driven pump 8 is connected with a first ball valve b901b, the first ball valve b901b is respectively connected with a second ball valve b902b and a third ball valve b903b, the second ball valve b902b is respectively connected with a fourth ball valve b904b, a seventh ball valve b907b and a tenth ball valve b910b, the third ball valve b903b is connected with a fifth ball valve b905b, the fifth ball valve b905b is respectively connected with a fourth ball valve b904b and a sixth ball valve b906b, the sixth ball valve b906b is connected with an eighth ball valve b908b, the eighth ball valve b908b is respectively connected with a seventh ball valve b907b and a ninth ball valve b909b, the ninth ball 909b is connected with an eleventh ball valve b911b, and the eleventh ball valve b911b is respectively connected with a tenth ball valve b910b and a twelfth ball valve 912 b;
In this embodiment, a connection manner of "series-parallel connection" is adopted, when the electric heater 9 portion works normally, the second ball valve b902b, the fourth ball valve b904b, the seventh ball valve b907b and the tenth ball valve b910b are closed, so that the sequential connection of the electric heaters 9 can be realized, when one of the electric heaters 9 fails, the ball valves at the two ends of the electric heater are closed, the corresponding ball valve above the electric heater is opened to communicate with the electric heater 9 and jump over the failed electric heater 9, so that the smoothness of the whole desorption electrolysis system is realized, and the normal desorption electrolysis operation is ensured.
Claims (5)
1. The utility model provides a high temperature high pressure desorption electrolysis system heater pipe-line device, its characterized in that, includes desorption post (1), desorption post (1) is connected with filter (2) through the pipeline, filter (2) are connected with electrolysis trough (5) through the pipeline, electrolysis trough (5) are connected with compensating tank (6), compensating tank (6) are connected with ball valve (7), ball valve (7) respectively with join in marriage cistern (3) and magnetic force actuation pump (8), magnetic force actuation pump (8) are connected with electric heater (9), electric heater (9) are connected with desorption post (1) and condenser (4) respectively through the pipeline, condenser (4) are connected with joining in marriage cistern (3).
2. A high temperature high pressure desorption electrolysis system heater pipe arrangement according to claim 1, wherein there are three electric heaters (9).
3. A high temperature high pressure desorption electrolysis system heater piping arrangement according to claim 2, wherein said three electric heaters (9) are connected in series.
4. The heater pipeline device for the high-temperature high-pressure desorption electrolysis system according to claim 2, wherein the magnetic force driven pump (8) is connected with a first ball valve a (901 a), the first ball valve a (901 a) is respectively connected with a second ball valve a (902 a) and a fourth ball valve a (904 a) through a pipeline, the second ball valve a (902 a) is respectively connected with a third ball valve a (903 a) and a sixth ball valve a (906 a) through a pipeline, the fourth ball valve a (904 a) is connected with a fifth ball valve a (905 a), the sixth ball valve a (906 a) is connected with a seventh ball valve a (907 a), the third ball valve a (903 a) is connected with an eighth ball valve a (908 a), and the eighth ball valve a (908 a) and the seventh ball valve a (907 a) are both connected with a ninth ball valve a (909 a);
electric heaters (9) are arranged between the fourth ball valve a (904 a) and the fifth ball valve a (905 a), between the sixth ball valve a (906 a) and the seventh ball valve a (907 a) and between the third ball valve a (903 a) and the eighth ball valve a (908 a).
5. The heater pipeline device for the high-temperature high-pressure desorption electrolysis system according to claim 2, wherein the magnetic force driven pump (8) is connected with a first ball valve b (901 b), the first ball valve b (901 b) is respectively connected with a second ball valve b (902 b) and a third ball valve b (903 b), the second ball valve b (902 b) is respectively connected with a fourth ball valve b (904 b), a seventh ball valve b (907 b) and a tenth ball valve b (910 b), the third ball valve b (903 b) is connected with a fifth ball valve b (905 b), the fifth ball valve b (905 b) is respectively connected with a fourth ball valve b (904 b) and a sixth ball valve b (906 b), the sixth ball valve b (906 b) is connected with an eighth ball valve b (908 b), the eighth ball valve b (908 b) is respectively connected with a seventh ball valve b (904 b) and a ninth ball valve b (909 b), the ninth ball valve b (909 b) is connected with an eleventh ball valve b (911 b) and a twelfth ball valve b (912 b);
electric heaters (9) are arranged between the third ball valve b (903 b) and the fifth ball valve b (905 b), between the sixth ball valve b (906 b) and the eighth ball valve b (908 b), and between the ninth ball valve b (909 b) and the eleventh ball valve b (911 b).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222321615.7U CN218642800U (en) | 2022-09-01 | 2022-09-01 | High-temperature high-pressure desorption electrolysis system heater pipeline device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222321615.7U CN218642800U (en) | 2022-09-01 | 2022-09-01 | High-temperature high-pressure desorption electrolysis system heater pipeline device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218642800U true CN218642800U (en) | 2023-03-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222321615.7U Active CN218642800U (en) | 2022-09-01 | 2022-09-01 | High-temperature high-pressure desorption electrolysis system heater pipeline device |
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| CN (1) | CN218642800U (en) |
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2022
- 2022-09-01 CN CN202222321615.7U patent/CN218642800U/en active Active
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