CN202876797U - Stainless steel reactor for processing ethylene glycol antimony - Google Patents
Stainless steel reactor for processing ethylene glycol antimony Download PDFInfo
- Publication number
- CN202876797U CN202876797U CN 201220502391 CN201220502391U CN202876797U CN 202876797 U CN202876797 U CN 202876797U CN 201220502391 CN201220502391 CN 201220502391 CN 201220502391 U CN201220502391 U CN 201220502391U CN 202876797 U CN202876797 U CN 202876797U
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- tank body
- stainless steel
- reductor
- support
- steel cauldron
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Abstract
The utility model discloses a stainless steel reactor for processing ethylene glycol antimony and relates to reactors. A motor (1) is arranged at the upper part of a speed reducer (2), the speed reducer is arranged at the upper end of an upper seal head (5) at the upper part of a tank body (18), a support (14) with a discharge port (15) is arranged on the inner bottom of the tank body, a bearing (13) is arranged on the support, the upper and lower ends of a rotating rod (6) are respectively connected with the speed reducer (2) and the bearing, and at least two stirring blades (12) with 'V'-shaped structures are arranged on an outer edge surface of a connecting sleeve (7) which is arranged at the lower part of the rotating rod; a heat accumulation cover (11) covers the tank body, a closed cavity is formed between the heat accumulation cover and the outer part of the tank body (18), and an air inlet valve (9) and an air release valve (10) are respectively arranged on the heat accumulation cover; and an emptying valve (17) is arranged on the tank body at the lower part of the support. By utilizing the stainless steel reactor, the reaction process safety is ensured, and the 'V'-shaped stirring blades can also completely stir ethylene glycol antimony in the tank bottom.
Description
[technical field]
The utility model relates to a kind of reactor, especially relates to a kind of antimony glycol processing stainless steel cauldron.
[background technology]
At present, what the additive of plastic products used is the catalytic antimony trioxide and antimony acetate, all has certain toxicity, because antimony glycol has preferably catalytic action, it is compared with antimony acetate with the catalytic antimony trioxide, and solubility is large in the ethylene glycol solution, good dispersion.Antimony content is high, and is active good, can improve plant capacity.Itself can not bring new impurity into this catalyst, can make section improve inherent quality, processing spinnability after improving.At present, the main component of the plastic bottle used of processing beverage, edible wet goods is polyester.In the manufacture process of polyester, need a kind of catalyst.Mostly adopted in the past the antimony-based catalyst " the catalytic antimony trioxide and antimony acetate " that contains poisonous heavy metal, especially after being heated, the possibility that toxin produces is larger.After using antimony glycol, can allow plastic bottle remove the cap that contains noxious material.But in the processing technology of antimony glycol, the control of temperature and the explosion-proof production overall process that runs through.Need firm insulation such as equipment such as reactor, crystallization kettle, distillation still and preheating cans.
[summary of the invention]
The deficiency that exists for overcoming prior art, the utility model provides a kind of antimony glycol processing stainless steel cauldron, being set to thickness by upper cover, tank body is 10 to 15 ㎜, guaranteed the security of heating for dissolving course of reaction, the utility model paddle is set to " V " shape, so that the antimony glycol at the bottom of the tank is also fully stirred.
For achieving the above object, the utility model adopts following technical scheme:
A kind of antimony glycol processing stainless steel cauldron, comprise tank body, motor, reductor, paddle, heat gathering cover, intake valve, air bleeding valve and baiting valve, motor is arranged on reductor top, described reductor is arranged on the upper cover upper end on tank body top, be provided with the support with discharge opening at the bottom of the tank in the tank body, support is provided with bearing, and the up and down two ends of bull stick connect respectively reductor, bearing, and the adapter sleeve outer edge surface that arranges in the bull stick bottom is provided with the paddle of at least two " V " shape structures; Heat gathering cover is wrapped in the outside of tank body, forms airtight cavity between the outside of heat gathering cover and tank body, is respectively equipped with intake valve, air bleeding valve on the heat gathering cover; Tank body in the support bottom is provided with baiting valve.
Stainless steel cauldron is used in described antimony glycol processing, is provided with adpting flange in the upper end of upper cover, and described adpting flange is connected with the adpting flange of frame, and reductor is arranged on the upper end of frame.
Stainless steel cauldron is used in described antimony glycol processing, is provided with adapter sleeve at the middle part of bull stick, and foreign aid's face of described adapter sleeve is provided with at least two blades.
Described antimony glycol processing stainless steel cauldron is provided with at least three supporting legs around the bottom of heat gathering cover.
It is 10 to 15 ㎜ that stainless steel cauldron, described upper cover, tank body thickness are used in described antimony glycol processing.
Owing to adopted technique scheme, of the present utility model have a following beneficial effect:
Antimony glycol processing stainless steel cauldron described in the utility model, being set to thickness by upper cover, tank body is 10 to 15 ㎜, guaranteed the security of heating for dissolving course of reaction, monoblock type heat gathering cover in the tank body outer setting, so that steam equiblibrium mass distribution in heat gathering cover, described paddle is set to " V " shape, so that the ethylene glycol at the bottom of the tank and raw material antimony are also fully stirred; The utility model sealing effectiveness and safe can be accelerated the course of reaction of ethylene glycol and raw material antimony effectively.
[description of drawings]
Fig. 1 is structural representation of the present utility model;
Among the figure: 1, motor; 2, reductor; 3, frame; 4, adpting flange; 5, upper cover; 6, bull stick; 7, adapter sleeve; 8, blade; 9, intake valve; 10, air bleeding valve; 11, heat gathering cover; 12, paddle; 13, bearing; 14, support; 15, discharge opening; 16, supporting leg; 17, baiting valve; 18, tank body.
[specific embodiment]
Can explain in more detail the utility model by the following examples, the utility model is not limited to the following examples, and open the purpose of this utility model is intended to protect all changes and improvements in the utility model scope;
1 described antimony glycol is processed and is used stainless steel cauldron by reference to the accompanying drawings, comprise tank body 18, motor 1, reductor 2, paddle 12, heat gathering cover 11, intake valve 9, air bleeding valve 10 and baiting valve 17, motor 1 is arranged on reductor 2 tops, be provided with adpting flange 4 in the upper end of upper cover 5, described adpting flange 4 is connected with the adpting flange 4 of frame 3, reductor 2 is arranged on the upper end of frame 3, be provided with the support 14 with discharge opening 15 at the bottom of the tank in the tank body 18, support 14 is provided with bearing 13, the up and down two ends of bull stick 6 connect respectively reductor 2, bearing 13, be provided with adapter sleeve 7 at the middle part of bull stick 6, foreign aid's face of described adapter sleeve 7 is provided with at least two blades 8, and adapter sleeve 7 outer edge surfaces that arrange in bull stick 6 bottoms are provided with the paddle 12 of at least two " V " shape structures; Heat gathering cover 11 is wrapped in the outside of tank body 18, form airtight cavity between the outside of heat gathering cover 11 and tank body 18, described upper cover 5, tank body 18 thickness are 10 to 15 ㎜, be respectively equipped with intake valve 9, air bleeding valve 10 at heat gathering cover 11, around the bottom of heat gathering cover 11, be provided with at least three supporting legs 16; Tank body 18 in support 14 bottoms is provided with baiting valve 17.
Implement antimony glycol processing stainless steel cauldron described in the utility model, ethylene glycol and raw material antimony are put into tank body 18, to vacuumize in the tank body 18, then starter motor 1, drive reductor 2, bull stick 6, blade 8 and paddle 12 by starter motor 1, open simultaneously intake valve 9, make tank body 18 form thermal field, so that ethylene glycol and raw material antimony catalytic reaction in high temperature are finally obtained antimony glycol.
The utility model does not describe part in detail and is prior art.
Claims (5)
1. an antimony glycol is processed and is used stainless steel cauldron, comprise tank body (18), motor (1), reductor (2), paddle (12), heat gathering cover (11), intake valve (9), air bleeding valve (10) and baiting valve (17), it is characterized in that: motor (1) is arranged on reductor (2) top, described reductor (2) is arranged on upper cover (5) upper end on tank body (18) top, be provided with the have discharge opening support (14) of (15) at the bottom of the tank in the tank body (18), support (14) is provided with bearing (13), the up and down two ends of bull stick (6) connect respectively reductor (2), bearing (13), adapter sleeve (7) outer edge surface that arranges in bull stick (6) bottom is provided with the paddle (12) of at least two " V " shape structures; Heat gathering cover (11) is wrapped in the outside of tank body (18), forms airtight cavity between the outside of heat gathering cover (11) and tank body (18), is respectively equipped with intake valve (9), air bleeding valve (10) on the heat gathering cover (11); Tank body (18) in support (14) bottom is provided with baiting valve (17).
2. antimony glycol according to claim 1 is processed and is used stainless steel cauldron, it is characterized in that: be provided with adpting flange (4) in the upper end of upper cover (5), described adpting flange (4) is connected with the adpting flange (4) of frame (3), and reductor (2) is arranged on the upper end of frame (3).
3. stainless steel cauldron is used in antimony glycol processing according to claim 1, and it is characterized in that: be provided with adapter sleeve (7) at the middle part of bull stick (6), foreign aid's face of described adapter sleeve (7) is provided with at least two blades (8).
4. stainless steel cauldron is used in antimony glycol processing according to claim 1, it is characterized in that: be provided with at least three supporting legs (16) around the bottom of heat gathering cover (11).
5. stainless steel cauldron is used in antimony glycol processing according to claim 1, and it is characterized in that: described upper cover (5), tank body (18) thickness are 10 to 15 ㎜.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220502391 CN202876797U (en) | 2012-09-28 | 2012-09-28 | Stainless steel reactor for processing ethylene glycol antimony |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220502391 CN202876797U (en) | 2012-09-28 | 2012-09-28 | Stainless steel reactor for processing ethylene glycol antimony |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202876797U true CN202876797U (en) | 2013-04-17 |
Family
ID=48068263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220502391 Expired - Fee Related CN202876797U (en) | 2012-09-28 | 2012-09-28 | Stainless steel reactor for processing ethylene glycol antimony |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202876797U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104096501A (en) * | 2014-07-23 | 2014-10-15 | 安庆市东徽机械有限公司 | Diluting kettle |
| CN108945551A (en) * | 2018-09-17 | 2018-12-07 | 河南叮当牛食品有限公司 | A kind of bulking system and technique |
-
2012
- 2012-09-28 CN CN 201220502391 patent/CN202876797U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104096501A (en) * | 2014-07-23 | 2014-10-15 | 安庆市东徽机械有限公司 | Diluting kettle |
| CN108945551A (en) * | 2018-09-17 | 2018-12-07 | 河南叮当牛食品有限公司 | A kind of bulking system and technique |
| CN108945551B (en) * | 2018-09-17 | 2023-08-15 | 河南叮当牛食品有限公司 | Filling system and process |
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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: 20130417 Termination date: 20170928 |