CN208865208U - Destilling tower is used in a kind of production of higher boiling coalescing agent - Google Patents

Destilling tower is used in a kind of production of higher boiling coalescing agent Download PDF

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Publication number
CN208865208U
CN208865208U CN201821481402.8U CN201821481402U CN208865208U CN 208865208 U CN208865208 U CN 208865208U CN 201821481402 U CN201821481402 U CN 201821481402U CN 208865208 U CN208865208 U CN 208865208U
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China
Prior art keywords
tower body
pipe
heating kettle
cooling cylinder
coalescing agent
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CN201821481402.8U
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Chinese (zh)
Inventor
张世元
张润赟
宋文国
杨萍
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Ruentex Chemical (taixing) Co Ltd
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Ruentex Chemical (taixing) Co Ltd
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Abstract

A kind of higher boiling coalescing agent production destilling tower, the utility model relates to chemical equipment technical field, the side of the heating kettle is equipped with adding mouth, and the upper end of adding mouth is screwed with case lid;The bottom of the heating kettle is equipped with No.1 drain pipe, is connected with No.1 valve on No.1 drain pipe;It is arranged with heater strip in the bottom of the heating kettle shell, side wall, heater strip is connect with external power supply;The side of the heating kettle is connected with diversion pipe, and the end of diversion pipe is set to the downside in tower body after passing through tower body side wall, and tower body is set to the outside of heating kettle;The bottom of the tower body is connected with No. two drain pipes, and No. two valves are connected on No. two drain pipes;Heating speed can be improved in circulating type heating, and vaporization efficency is higher, enhances heat-conducting effect, chilled contact area is increased in condensation process, and can reinforce condensation rate, can also supply electrical equipment using the electric energy that solar energy generates, practical.

Description

Destilling tower is used in a kind of production of higher boiling coalescing agent
Technical field
The utility model relates to chemical equipment technical fields, and in particular to a kind of higher boiling coalescing agent production distillation Tower.
Background technique
Destilling tower is the chemical industry equipment of the materials such as rare metal titanium and its alloy material manufacture, have intensity is high, toughness is big, The characteristics such as high temperature resistant, corrosion-resistant, light specific gravity;The principle of destilling tower is separated according to the gap of boiling point of liquid, equipment Working principle is that the gas risen by lower layer transfers heat to supernatant liquid and is allowed to vaporize, therefore is widely used and changes The fields such as work, petrochemical industry, metallurgy, light industry, weaving, alkaline, pharmacy, pesticide, plating, electronics.Coalescing agent is also known as coalesced and is helped Agent can promote high-molecular compound Plastic Flow and flexible deformation, improve coalescence performance, can be within the scope of wide construction temperature The substance of film forming;Coalescing agent needs to carry out distillation extraction by destilling tower;Adding in the destilling tower of existing coalescing agent Thermal velocity is slow, and heating efficiency is low, and heat-conducting effect is also bad, and condensation efficiency is not high, it would be highly desirable to improve.
Utility model content
The purpose of this utility model is that in view of the drawbacks of the prior art and insufficient, provide that a kind of structure is simple, and design is closed Heating speed can be improved in reason, higher boiling coalescing agent easy to use production destilling tower, circulating type heating, and vaporization efficency is more Height enhances heat-conducting effect, chilled contact area is increased in condensation process, and can reinforce condensation rate, can be with benefit Electrical equipment is supplied with the electric energy that solar energy generates, it is practical.
In order to achieve the above purposes, the technical solution adopted by the utility model is:, and it includes heating kettle, No.1 drain pipe, leads Flow tube, tower body, baffle, inclined plate, cooling cylinder, condenser pipe, collecting box, heat-preservation cotton;The side of the heating kettle is equipped with adding mouth, The upper end of adding mouth is screwed with case lid;The bottom of the heating kettle is equipped with No.1 drain pipe, is connected with one on No.1 drain pipe Number valve;It is arranged with heater strip in the bottom of the heating kettle shell, side wall, heater strip is connect with external power supply;It is described The side of heating kettle be connected with diversion pipe, the end of diversion pipe is set to the downside in tower body after passing through tower body side wall, and tower body is set In the outside of heating kettle;The bottom of the tower body is connected with No. two drain pipes, and No. two valves are connected on No. two drain pipes;Institute The inside for the tower body stated is fixed with several baffles from bottom to up, and circumference isogonism is equipped with several grooves, gear from bottom to up on baffle Groove on plate shifts to install up and down, and baffle is equipped with several air holes;Top in the tower body is fixed with inclined plate, tower body Outside be equipped with cooling cylinder, water inlet pipe is connected on the upside of cooling cylinder, water inlet pipe is connect with outside supply equipment, under cooling cylinder Side is connected with outlet pipe, and outlet pipe is connect with exterior drain;Condenser pipe is equipped in the cooling cylinder, condensation pipe dish is located at In cooling cylinder, the upper end of condenser pipe is connect after passing through cooling cylinder side wall with tower body;The lower end of the condenser pipe passes through cooling cylinder Bottom plate after connect with collecting box, collecting box is fixed on the outside of tower body by fixed ring;The collecting box is infundibulate knot Structure, the bottom of collecting box are connected with No. three drain pipes, No. three valves are connected on No. three drain pipes;The heating kettle, water conservancy diversion Pipe, tower body, cooling cylinder outside be wrapped with heat-preservation cotton, heating kettle, tower body bottom be respectively and fixedly provided with support foot.
Further, the heater strip is connect with the battery for being set to heating kettle side, battery and solar battery Component connection, solar cell module are set to outdoor.
Further, explosion-proof cloth is wrapped on the outside of the cooling cylinder.
Further, thermally conductive layer of paste is folded between the heater strip and heating kettle inner wall.
Further, the No.1 drain pipe, No. two drain pipes inner wall be respectively and fixedly provided with strainer, strainer is respectively arranged on one The downside of number valve, No. two valves.
After adopting the above structure, the utility model has the beneficial effect that a kind of higher boiling film forming described in the utility model helps Heating speed can be improved in agent production destilling tower, circulating type heating, and vaporization efficency is higher, enhances heat-conducting effect, condenses Chilled contact area is increased in journey, and can reinforce condensation rate, can also be supplied using the electric energy that solar energy generates The advantages that electrical equipment, practical, the utility model has structure simple, is arranged rationally, low manufacture cost.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the schematic diagram of the utility model.
Fig. 2 is the cross-sectional view of the utility model.
Fig. 3 is the schematic diagram of baffle in the utility model.
Fig. 4 is the cross-sectional view in the portion A in Fig. 2.
Fig. 5 is the schematic diagram of solar cell module in the utility model.
Description of symbols:
Heating kettle 1, adding mouth 1-1, case lid 1-2, heater strip 1-3, No.1 drain pipe 2, No.1 valve 2-1, diversion pipe 3, 4, No. two drain pipe 4-1 of tower body, No. two valve 4-2, baffle 5, groove 5-1, air hole 5-2, inclined plate 6, cooling cylinder 7, water inlet pipe It is 7-1, outlet pipe 7-2, condenser pipe 8,9, No. three drain pipe 9-1 of collecting box, No. three valve 9-2, heat-preservation cotton 10, strainer 11, explosion-proof Cloth 12, thermally conductive layer of paste 13, battery 14, solar cell module 15, support foot 16.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings.
Referring to as shown in Figures 1 to 5, technological means used by present embodiment is as follows: it include heating kettle 1, No.1 drain pipe 2, diversion pipe 3, tower body 4, baffle 5, inclined plate 6, cooling cylinder 7, condenser pipe 8, collecting box 9, heat-preservation cotton 10;Described The side of heating kettle 1 is screwed with case lid 1-2 integrally formed with adding mouth 1-1, the upper end of adding mouth 1-1, is added from adding mouth 1-1 The coalescing agent to be distilled, case lid 1-2 can keep the sealing of heating kettle 1 during heating;The bottom of the heating kettle 1 Integrally formed with No.1 drain pipe 2, No.1 valve 2-1 has been connected through a screw thread on No.1 drain pipe 2, it, can be with after distillation Control remaining material in No.1 valve 2-1 discharge heating kettle 1;Be arranged in the bottom of 1 shell of heating kettle, side wall plus Heated filament 1-3, heater strip 1-3 are connect with external power supply, and heater strip 1-3 is wound around surrounding side wall and the bottom of heating kettle 1, can be with Accelerate heating speed, distillation speed can be accelerated;The side of the heating kettle 1 is welded and connected with diversion pipe 3, diversion pipe 3 End is set to the downside in tower body 4 after passing through 4 side wall of tower body, and with tower body 4 by being welded and fixed, coalescing agent vaporizes diversion pipe 3 After can along diversion pipe 3 enter tower body 4, tower body 4 be set to heating kettle 1 outside;The bottom of the tower body 4, which is integrally formed, to be connected It is connected on No. two drain pipes 4-1, No. two drain pipe 4-1 and has been connected through a screw thread No. two valve 4-2, can be discharged in tower body 4 Liquefied coalescing agent;The inside of the tower body 4 is welded and fixed from bottom to up there are four baffle 5, be integrally formed on baffle 5 and Circumference isogonism is set there are three groove 5-1, and the groove 5-1 or more on baffle 5 from bottom to up is shifted to install, can be slowed down film forming and help The rate of climb under agent vapor state, increase with the contact of baffle 5, integrally formed with 46 air hole 5-2 on baffle 5, The rate of climb under coalescing agent vapor state is further slowed down, coalescing agent can be allowed to be dropped during rising Temperature;Top in the tower body 4 is welded with inclined plate 6, and inclined plate 6 can provide guiding role to coalescing agent, so that at Film auxiliary agent is moved toward 8 direction of condenser pipe, and the outside of tower body 4 is equipped with cooling cylinder 7, the upside of cooling cylinder 7 be integrally formed be connected with into Water pipe 7-1, water inlet pipe 7-1 are connect with external supply equipment, and the downside of cooling cylinder 7, which is integrally formed, is connected with outlet pipe 7-2, are discharged Pipe 7-2 is connect with exterior drain, is formed a Water-cooling circulating, can be condensed rapidly, so that the coalescing agent of vaporization Liquefaction rapidly;Condenser pipe 8 is equipped in the cooling cylinder 7,8 disk of condenser pipe is located in cooling cylinder 7, and the upper end of condenser pipe 8 passes through It is connect after 7 side wall of cooling cylinder with tower body 4, the coalescing agent of vaporization can enter condenser pipe 8 out of tower body 4, enter along condenser pipe 8 Cooling cylinder 7;The lower end of the condenser pipe 8 is connect after the bottom plate of cooling cylinder 7 with collecting box 9, and collecting box 9 passes through fixed ring It is fixed on the outside of tower body 4, Fixing shrink ring is located at 9 outside of collecting box, and is weldingly fixed on 4 outside of tower body, the film forming after liquefaction Auxiliary agent can flow into collecting box 9 from condenser pipe 8;The collecting box 9 is funnel-shaped structure, and coalescing agent is facilitated to be discharged, and is collected The bottom of case 9, which is integrally formed to be connected on No. three drain pipes 9-1, No. three drain pipe 9-1, has been connected through a screw thread No. three valve 9- 2, coalescing agent discharge can be controlled by No. three valve 9-2;The heating kettle 1, diversion pipe 3, tower body 4, cooling cylinder 7 it is outer Side is wrapped with heat-preservation cotton 10, there is insulation effect, and heating speed faster, prevents coalescing agent to be also less than 4 inside of tower body and just liquefies, Heating kettle 1, tower body 4 bottom be welded with support foot 16.
Further, the heater strip 1-3 connect with the battery 14 for being set to 1 side of heating kettle, battery 14 and too Positive energy battery component 15 connects, and solar cell module 15 is set to outdoor, and solar cell module 15 can use solar energy and turn Electric energy is turned to, is stored into battery 14 and is used for heater strip 1-3, it is possible to reduce the cost of distillation.
Further, the outside of the cooling cylinder 7 is wrapped with explosion-proof cloth 12, and explosion-proof cloth 12 is high-strength high-modulo ultra-high molecular Weight polyethylene fiber UD cloth and woven fabric composition, prevent cooling cylinder 7 from bursting open to lead to accident injury, can wrap to a certain extent It wraps cooling cylinder 7 and prevents from bursting and come.
Further, thermally conductive layer of paste 13, thermally conductive layer of paste 13 are folded between 1 inner wall of the heater strip 1-3 and heating kettle For thermal conductive silicon fat, the heat that heater strip 1-3 is generated can quickly be led inside heating kettle 1.
Further, the equal gluing of inner wall of 2, No. two drain pipe 4-1 of the No.1 drain pipe is fixed with strainer 11, strainer 11 are respectively arranged on the downside of No.1 valve 2-1, No. two valve 4-2, can carry out to the coalescing agent that do not distill sufficiently of discharge Filtering.
The working principle of this specific embodiment: being: the coalescing agent for needing to distill being added from adding mouth 1-1, by case lid 1- 2 are tightened by screw thread, and heater strip 1-3 is begun to warm up after powering on, and heat can quickly be transmitted to heating by thermally conductive layer of paste 13 In kettle 1, after the temperature in heating kettle 1 reaches the boiling point in coalescing agent, coalescing agent will become vapor state, vaporization at Film auxiliary agent can rise, and into diversion pipe 3, enter tower body 4 along diversion pipe 3, begin to ramp up movement from the downside in tower body 4, on During elevator is dynamic, by the obstruction of four baffles 5, the rate of climb can slow down, and temperature can also be fallen, and part coalescing agent can be first Liquefaction drops onto 4 bottom of tower body, some coalescing agent is not by also dropping to boiling point hereinafter, will continue to after baffle 5 It rises, after touching inclined plate 6, condenser pipe 8 can be entered along inclined plate 6, enter cooling cylinder 7 along condenser pipe 8, pass through in cooling cylinder 7 Water inlet pipe 7-1, outlet pipe 7-2 are always maintained at dampening circulation, and coalescing agent liquefies after dropping to boiling point or less in cooling cylinder 7, The coalescing agent of liquid can drop onto collecting box 9 out of condenser pipe 8, due to the funnel-shaped structure of collecting box 9, coalescing agent meeting It is flow to 9 bottom of collecting box, by controlling No. three valve 9-2, the coalescing agent after distillation can be discharged from No. three drain pipe 9-1, It, can be by controlling No.1 valve 2-1, from No.1 drain pipe 2 through filtering for the coalescing agent of vaporization in heating kettle 1 after distillation Net 11 is discharged, and first liquefied coalescing agent can be by controlling No. two valve 4-2, from No. two drain pipe 4-1 through strainer in tower body 4 11 discharges.
The technological merit of present embodiment are as follows: a kind of higher boiling coalescing agent that present embodiment is proposed is raw It produces and uses destilling tower, heating speed can be improved in circulating type heating, and vaporization efficency is higher, heat-conducting effect is enhanced, in condensation process Chilled contact area is increased, and condensation rate can be reinforced, electricity consumption can also be supplied using the electric energy that solar energy generates Equipment, it is practical, have structure simple, setting rationally, the advantages that low manufacture cost.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model Spirit and scope should all cover in the scope of the claims of the utility model.

Claims (5)

1. a kind of higher boiling coalescing agent production destilling tower, it is characterised in that: it includes heating kettle (1), No.1 drain pipe (2), diversion pipe (3), tower body (4), baffle (5), inclined plate (6), cooling cylinder (7), condenser pipe (8), collecting box (9), heat-preservation cotton (10);The side of the heating kettle (1) is equipped with adding mouth (1-1), and the upper end of adding mouth (1-1) is screwed with case lid (1-2);Institute The bottom for the heating kettle (1) stated is equipped with No.1 drain pipe (2), is connected with No.1 valve (2-1) on No.1 drain pipe (2);It is described The bottom of heating kettle (1) shell, be arranged with heater strip (1-3) in side wall, heater strip (1-3) is connect with external power supply;Institute The side for the heating kettle (1) stated is connected with diversion pipe (3), and the end of diversion pipe (3) is set to tower body after passing through tower body (4) side wall (4) downside in, tower body (4) are set to the outside of heating kettle (1);The bottom of the tower body (4) is connected with No. two drain pipe (4- 1) No. two valves (4-2), are connected on No. two drain pipes (4-1);The inside of the tower body (4) is fixed with several from bottom to up Baffle (5), circumference isogonism is equipped with several grooves (5-1) on baffle (5), and the groove (5-1) on baffle (5) from bottom to up is up and down It shifts to install, baffle (5) is equipped with several air holes (5-2);Top in the tower body (4) is fixed with inclined plate (6), tower body (4) outside is equipped with cooling cylinder (7), is connected with water inlet pipe (7-1) on the upside of cooling cylinder (7), water inlet pipe (7-1) and external water supply Equipment connects, and is connected with outlet pipe (7-2) on the downside of cooling cylinder (7), outlet pipe (7-2) is connect with exterior drain;It is described Cooling cylinder (7) in be equipped with condenser pipe (8), condenser pipe (8) disk is located in cooling cylinder (7), and the upper end of condenser pipe (8) passes through condensation It is connect after case (7) side wall with tower body (4);The lower end of the condenser pipe (8) pass through cooling cylinder (7) bottom plate after with collecting box (9) it connects, collecting box (9) is fixed on the outside of tower body (4) by fixed ring;The collecting box (9) is funnel-shaped structure, is received The bottom of header (9) is connected with No. three drain pipes (9-1), and No. three valves (9-2) are connected on No. three drain pipes (9-1);It is described Heating kettle (1), diversion pipe (3), tower body (4), cooling cylinder (7) outside be wrapped with heat-preservation cotton (10), heating kettle (1), tower The bottom of body (4) is respectively and fixedly provided with support foot (16).
2. a kind of higher boiling coalescing agent production destilling tower according to claim 1, it is characterised in that: the heating Silk (1-3) is connect with the battery (14) for being set to heating kettle (1) side, and battery (14) and solar cell module (15) are even It connects, solar cell module (15) is set to outdoor.
3. a kind of higher boiling coalescing agent production destilling tower according to claim 1, it is characterised in that: the condensation Explosion-proof cloth (12) are wrapped on the outside of case (7).
4. a kind of higher boiling coalescing agent production destilling tower according to claim 1, it is characterised in that: the heating Thermally conductive layer of paste (13) are folded between silk (1-3) and heating kettle (1) inner wall.
5. a kind of higher boiling coalescing agent production destilling tower according to claim 1, it is characterised in that: the No.1 Drain pipe (2), No. two drain pipes (4-1) inner wall be respectively and fixedly provided with strainer (11), strainer (11) is respectively arranged on No.1 valve (2- 1), the downside of No. two valves (4-2).
CN201821481402.8U 2018-09-11 2018-09-11 Destilling tower is used in a kind of production of higher boiling coalescing agent Active CN208865208U (en)

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Application Number Priority Date Filing Date Title
CN201821481402.8U CN208865208U (en) 2018-09-11 2018-09-11 Destilling tower is used in a kind of production of higher boiling coalescing agent

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110304773A (en) * 2019-05-20 2019-10-08 湖南杰安环保设备有限公司 A kind of industrial large-flow water purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110304773A (en) * 2019-05-20 2019-10-08 湖南杰安环保设备有限公司 A kind of industrial large-flow water purifier

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