CN205329213U - Automatic carminative diphenyl heat preservation system - Google Patents
Automatic carminative diphenyl heat preservation system Download PDFInfo
- Publication number
- CN205329213U CN205329213U CN201620075135.9U CN201620075135U CN205329213U CN 205329213 U CN205329213 U CN 205329213U CN 201620075135 U CN201620075135 U CN 201620075135U CN 205329213 U CN205329213 U CN 205329213U
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- Prior art keywords
- diphenyl
- biphenyl
- exhaust tank
- tank
- air inlet
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Abstract
The utility model provides an automatic carminative diphenyl heat preservation system, including a diphenyl boiler, a plurality of box that is used for holding the section fuse -element, an exhaust tank, a temperature sensor, a diphenyl storage tank, an and temperature controller, diphenyl boiler is connected respectively through an air inlet pipeline and each box, the box is given vent to anger the pipeline through one and is connected with the air inlet of exhaust tank, the gas vent of exhaust tank is connected with the diphenyl storage tank through a blast pipe, the backward flow mouth of exhaust tank is connected with diphenyl boiler through a back flow, the diphenyl storage tank is connected with diphenyl boiler through a conveyer pipe, and be equipped with a delivery pump on this conveyer pipe, temperature sensor installs in the air inlet department of exhaust tank, be equipped with a electromagnetic valves on the blast pipe, electromagnetic valves, temperature sensor is connected with the temperature controller respectively. The utility model discloses can realize self -bleeding to reduce operating personnel's work load in the very big degree, and avoided diphenyl heat preservation system temperature's deviation, guaranteed the quality of product.
Description
[technical field]
This utility model belongs to the device systems in spinning field, is specifically related to a kind of self-bleeding biphenyl heat-insulation system。
[background technology]
In spinning production process, in order to ensure the temperature of section melt, it is generally adopted biphenyl heat-insulation system and section melt is incubated。Existing biphenyl heat-insulation system generally includes a diphenyl boiler, a plurality of casings for holding section melt, one exhaust tank, one temperature sensor, and a biphenyl storage tank, diphenyl boiler is connected with each casing respectively by air inlet pipeline, casing is connected with the air inlet of exhaust tank by outlet pipe, the air vent of exhaust tank is connected with biphenyl storage tank by exhaustor, the refluxing opening of exhaust tank is connected with diphenyl boiler by return duct, biphenyl storage tank is connected with diphenyl boiler by a conveying pipe, and this conveying pipe is provided with delivery pump, temperature sensor is installed on the air inlet place of exhaust tank, escape pipe is provided with manually-operated gate。
Wherein, diphenyl boiler becomes biphenyl steam by after liquid biphenyl heating and gasifying, and biphenyl steam enters casing and section melt is incubated；When the temperature in exhaust tank is lower than 240 DEG C (250 DEG C of room temperature biphenyl, 240 DEG C of low temperature biphenyl) or when exhaust tank temperature substantially reduces, then mean system pipeline is deposited unknown gas, now need to manually start manually-operated gate to be exhausted, the temperature of guarantee system；And in spinning production process, spin manifold temperature requires to control within the range of error of 2 DEG C of setting value, therefore require that whether the every temperature patrolling and examining a biphenyl heat-insulation system for 2 hours of operator is normal, if it find that the temperature in exhaust tank is lower than 240 DEG C or when exhaust tank temperature substantially reduces, it is necessary to the timely aerofluxus of operator。Namely existing biphenyl heat-insulation system needs patrolling and examining of operator's timing, goes to exhaust tank aerofluxus continually, while adding workload to operator, there is also the deviation of biphenyl heat-insulation system temperature, have influence on the quality of product。
[utility model content]
Technical problem to be solved in the utility model is in that to provide a kind of self-bleeding biphenyl heat-insulation system, it is capable of automatic vent, thus reducing the workload of operator largely, and avoid the deviation of biphenyl heat-insulation system temperature, it is ensured that the quality of product。
This utility model is to solve above-mentioned technical problem by the following technical programs: a kind of self-bleeding biphenyl heat-insulation system, including a diphenyl boiler, a plurality of for holding the section casing of melt, an exhaust tank, a temperature sensor, a biphenyl storage tank and a temperature controller；Described diphenyl boiler is connected with each casing respectively by an air inlet pipeline, described casing is connected with the air inlet of exhaust tank by an outlet pipe, the air vent of described exhaust tank is connected with biphenyl storage tank by an exhaustor, the refluxing opening of described exhaust tank is connected with diphenyl boiler by a return duct, described biphenyl storage tank is connected with diphenyl boiler by a conveying pipe, and this conveying pipe is provided with a delivery pump, described temperature sensor is installed on the air inlet place of exhaust tank, described exhaustor is provided with an electromagnetic valve, described electromagnetic valve, temperature sensor is connected with temperature controller respectively。
Further, the number of described casing is 3。
Having the beneficial effects that of a kind of self-bleeding biphenyl heat-insulation system of this utility model: by setting up of temperature controller and coordinating of electromagnetic valve, it is capable of automatic vent, without operator timing patrol and examine, frequent aerofluxus, thus reducing the workload of operator largely, and can be real-time monitoring exhaust tank in temperature and timely automated aerofluxus, avoid the deviation of biphenyl heat-insulation system temperature, it is ensured that the quality of product。
[accompanying drawing explanation]
The utility model will be further described in conjunction with the embodiments with reference to the accompanying drawings。
Fig. 1 is the schematic diagram of a kind of self-bleeding biphenyl heat-insulation system of this utility model。
[detailed description of the invention]
Referring to Fig. 1, a kind of self-bleeding biphenyl heat-insulation system of this utility model, including a diphenyl boiler 1, a plurality of casing 2, exhaust tank 3, temperature sensor 4, biphenyl storage tank 5 for holding section melt and a temperature controller 6；Diphenyl boiler 1 is in order to form biphenyl steam by biphenyl liquid heating and gasifying, and temperature sensor 4 is in order to sense the temperature in detection exhaust tank 3, the gas that biphenyl storage tank 5 gives off for the standby biphenyl liquid of temporary transient storage and exhaust tank 3。
Diphenyl boiler 1 is connected with each casing 2 respectively by an air inlet pipeline 71, described casing 2 is connected with the air inlet 31 of exhaust tank 3 by an outlet pipe 72, the air vent 32 of described exhaust tank 3 is connected with biphenyl storage tank 5 by an exhaustor 73, the refluxing opening 33 of described exhaust tank 3 is connected with diphenyl boiler 1 by a return duct 74, described biphenyl storage tank 5 is connected with diphenyl boiler 1 by a conveying pipe 75, and this conveying pipe 75 is provided with a delivery pump 8, described temperature sensor 4 is installed on air inlet 31 place of exhaust tank 3, described exhaustor 73 is provided with an electromagnetic valve 9, described electromagnetic valve 9, temperature sensor 4 is connected with temperature controller 6 respectively。Wherein the concrete number of casing 2 is determined according to production line, and for productivity effect, most cases arranges 8 or 12 after class, in the present embodiment, in order to facilitate the concrete number of casing 2 to be 3。
During this utility model application, biphenyl steam will be formed after biphenyl liquid heating and gasifying by diphenyl boiler 1, biphenyl steam is entered in each casing 2 by air inlet pipeline 71 and section melt is incubated, and biphenyl steam is by flowing in exhaust tank 3 via outlet pipe 72 afterwards；When the temperature in exhaust tank 3 is not less than 240 DEG C, temperature controller 6 receives signal that temperature sensor 4 sends and controls electromagnetic valves 9 and be in the state of closedown, and the biphenyl steam entered in exhaust tank 3 condensation does not occur and is directly back to diphenyl boiler 1 via refluxing opening 33, return duct 74；When the temperature in exhaust tank 3 is lower than 240 DEG C or during suddenly significant hypothermal, enter the biphenyl vapor portion generation condensation in exhaust tank 3, then except biphenyl steam, also form part biphenyl liquid in exhaust tank 3, now temperature controller 6 receives signal that temperature sensor 4 sends and controls electromagnetic valves 9 and turn on, biphenyl steam flows into exhaustor 73 via air vent 32 and discharges to biphenyl storage tank 5, and the biphenyl liquid formed then drops down onto bottom exhaust tank 3 and enters return duct 74 via refluxing opening 33 and is back to diphenyl boiler 1；And it should be noted that when biphenyl amount of liquid deficiency in diphenyl boiler 1, then open delivery pump 8, make the biphenyl liquid of storage in biphenyl storage tank 5 send in diphenyl boiler 1 via conveying pipe 75。
To sum up, this utility model biphenyl heat-insulation system is capable of automatic vent, without operator timing patrol and examine, frequent aerofluxus, thus reducing the workload of operator largely, and can be real-time monitoring exhaust tank in temperature and timely automated aerofluxus, avoid the deviation of biphenyl heat-insulation system temperature, it is ensured that the quality of product。
Claims (2)
1. a self-bleeding biphenyl heat-insulation system, including a diphenyl boiler, a plurality of for holding the section casing of melt, an exhaust tank, a temperature sensor and a biphenyl storage tank；Described diphenyl boiler is connected with each casing respectively by an air inlet pipeline, described casing is connected with the air inlet of exhaust tank by an outlet pipe, the air vent of described exhaust tank is connected with biphenyl storage tank by an exhaustor, the refluxing opening of described exhaust tank is connected with diphenyl boiler by a return duct, described biphenyl storage tank is connected with diphenyl boiler by a conveying pipe, and this conveying pipe is provided with a delivery pump, described temperature sensor is installed on the air inlet place of exhaust tank；It is characterized in that: this biphenyl heat-insulation system also includes a temperature controller, described exhaustor is provided with an electromagnetic valve, and described electromagnetic valve, temperature sensor are connected with temperature controller respectively。
2. the self-bleeding biphenyl heat-insulation system of one according to claim 1, it is characterised in that: the number of described casing is 3。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620075135.9U CN205329213U (en) | 2016-01-26 | 2016-01-26 | Automatic carminative diphenyl heat preservation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620075135.9U CN205329213U (en) | 2016-01-26 | 2016-01-26 | Automatic carminative diphenyl heat preservation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205329213U true CN205329213U (en) | 2016-06-22 |
Family
ID=56318588
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620075135.9U Expired - Fee Related CN205329213U (en) | 2016-01-26 | 2016-01-26 | Automatic carminative diphenyl heat preservation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205329213U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109137109A (en) * | 2018-09-18 | 2019-01-04 | 江苏德力化纤有限公司 | A kind of porous POY production equipment of the thick denier of multi H shape and preparation method thereof |
| CN112522795A (en) * | 2020-11-27 | 2021-03-19 | 盐城市顺驰机械科技有限公司 | Spunbonded nonwoven box |
| CN109371476B (en) * | 2018-08-20 | 2021-08-10 | 宁波卓成化纤有限公司 | Temperature control method by using temperature control system with multipoint temperature difference of one biphenyl furnace |
-
2016
- 2016-01-26 CN CN201620075135.9U patent/CN205329213U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109371476B (en) * | 2018-08-20 | 2021-08-10 | 宁波卓成化纤有限公司 | Temperature control method by using temperature control system with multipoint temperature difference of one biphenyl furnace |
| CN109137109A (en) * | 2018-09-18 | 2019-01-04 | 江苏德力化纤有限公司 | A kind of porous POY production equipment of the thick denier of multi H shape and preparation method thereof |
| CN112522795A (en) * | 2020-11-27 | 2021-03-19 | 盐城市顺驰机械科技有限公司 | Spunbonded nonwoven box |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160622 Termination date: 20210126 |