CN105617973A - Petrochemical product production equipment - Google Patents
Petrochemical product production equipment Download PDFInfo
- Publication number
- CN105617973A CN105617973A CN201610145950.2A CN201610145950A CN105617973A CN 105617973 A CN105617973 A CN 105617973A CN 201610145950 A CN201610145950 A CN 201610145950A CN 105617973 A CN105617973 A CN 105617973A
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- CN
- China
- Prior art keywords
- stirred autoclave
- solid
- stirring
- reaction kettle
- liquid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
- B01D36/045—Combination of filters with centrifugal separation devices
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
Abstract
The invention discloses petrochemical product production equipment. The petrochemical product production equipment comprises a stirring reaction kettle which is internally provided with a stirring shaft, stirring impellers are arranged on the stirring shaft, a gearbox is connected to the upper end of the stirring shaft, a motor is installed on the gearbox, a feed port is formed in the upper end of the stirring reaction kettle, a booster pump is arranged on one side of the upper end of the stirring reaction kettle, a thermal insulation device is arranged on the outer side of the stirring reaction kettle, a discharge port is formed in the lower end of the stirring reaction kettle, the stirring reaction kettle is connected with a solid-liquid centrifugal separator through the discharge port, a filter box is connected to the upper end of the solid-liquid centrifugal separator, a solid phase discharge pipe is arranged at the lower end of the solid-liquid centrifugal separator, and a liquid phase discharge pipe is arranged at the lower end of the filter box. The petrochemical product production equipment is novel in structure, needed conditions during a reaction are met, the reaction speed is increased, the production efficiency is improved, the raw materials are fully stirred to be subjected to a full reaction, a solid phase and a liquid phase can be separated after the reaction, the liquid phase is further purified, the production efficiency is improved, the production cost is reduced, and the production requirements are met.
Description
Technical field
The present invention relates to a kind of petrochemical equipment, specifically a kind of petrochemicals production unit.
Background technology
Whipping device is extremely extensive in the application of the industries such as chemical industry, light industry, petrochemical industry, pharmacy, biology, its counter structure form is also rich and varied, its reasonable selection, can not only save energy, reduce production cost, also be ensure constant product quality a key factor. Traditional single shaft whipping device, is often only applicable to specific technical process. Along with the severization of processing requirement, this kind of function singleness, the simple whipping device of structure, more and more can not adapt to the diversified demand of big industrial production. It is that during the process industrial of representative is produced, chemical reaction complicated and changeable is very common, and these reaction process often change with phase, heat transmission and viscosity B coefficent etc. taking chemical industry, corresponding in different step of reaction, whipping device is proposed different requirements. Especially relating to the occasion of polyreaction, its system physical property changes very greatly, and often shows following feature: initial reaction stage, and agitated medium is the mixing of liquid-liquid low viscosity; Along with the carrying out of reaction, reactant precipitates out solids or generates high adhesive material, and system also becomes sticky thick gradually; In the reaction later stage, agitated medium is the full-bodied mixing of solid-liquid. For such polymerization reaction system, existing stirring and processing device, after stirring reaction, solid phase is together with liquid-phase mixing, and discharging is also mixture, lacks now and a kind of collection stirs and be separated equipment integrally.
Summary of the invention
It is an object of the invention to provide a kind of petrochemicals production unit, to solve in above-mentioned background technology the problem proposed.
For achieving the above object, the present invention provides following technical scheme:
A kind of petrochemicals production unit, comprise stirred autoclave, described stirred autoclave is provided with stir shaft, described stir shaft is provided with paddle wheel, stir shaft upper end connects wheel box, described wheel box is equipped with motor, described stirred autoclave upper end is provided with opening for feed, side, described stirred autoclave upper end is provided with topping-up pump, outside described stirred autoclave, attemperator is housed, the lower end of described stirred autoclave is provided with discharge port, described stirred autoclave connects solid liquid centrifuge separator by discharge port, described solid liquid centrifuge separator upper end connects strumbox, the described solid lower end of liquid centrifuge separator is provided with solid phase discharging pipe, the lower end of described strumbox is provided with liquid phase discharging pipe.
As the scheme that the present invention is further: described stirred autoclave upper end is provided with tensimeter.
As the scheme that the present invention is further: described topping-up pump is contained in side, stirred autoclave upper end by support.
As the scheme that the present invention is further: described attemperator comprises insulation can, described insulation can upper end is provided with water outlet, and the lower end of described insulation can is provided with water-in.
As the scheme that the present invention is further: described strumbox is provided with multistorey strainer mesh.
Compared with prior art, the invention has the beneficial effects as follows: present configuration is novel, by the design of attemperator and topping-up pump, meet the condition required when reacting, accelerate speed of response, improve production efficiency, the design of stir shaft and paddle wheel, fully stirs raw material, makes it abundant reaction, again by the design of solid liquid centrifuge separator and strumbox, make can be separated after the reaction solid phase and liquid phase, liquid phase of purifying further, it is to increase production efficiency, reduce production cost, meet production requirement.
Accompanying drawing explanation
Fig. 1 is the structural representation of petrochemicals production unit.
In figure: 1-strumbox, 2-filter screen, 3-solid liquid centrifuge separator, 4-paddle wheel, 5-stir shaft, 6-water outlet, 7-support, 8-topping-up pump, 9-wheel box, 10-motor, 11-tensimeter, 12-opening for feed, 13-stirred autoclave, 14-insulation can, 15-leg, 16-discharge port.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is only the present invention's part embodiment, instead of whole embodiments. Based on the embodiment in the present invention, those of ordinary skill in the art, not making other embodiments all obtained under creative work prerequisite, belong to the scope of protection of the invention.
Refer to Fig. 1, in the embodiment of the present invention, a kind of petrochemicals production unit, comprise stirred autoclave 13, stirred autoclave 13 is provided with stir shaft 5, stir shaft 5 is provided with paddle wheel 4, stir shaft 5 upper end connects wheel box 9, wheel box 9 is equipped with motor 10, stirred autoclave 13 upper end is provided with opening for feed 12, side, stirred autoclave 13 upper end is provided with topping-up pump 8, outside stirred autoclave 13, attemperator is housed, stirred autoclave 13 times ends are provided with discharge port 16, stirred autoclave 13 connects solid liquid centrifuge separator 3 by discharge port 16, Gu liquid centrifuge separator 3 upper end connects strumbox 1, Gu liquid centrifuge separator 3 times ends are provided with solid phase discharging pipe, strumbox 1 time end is provided with liquid phase discharging pipe, stirred autoclave 13 upper end is provided with tensimeter 11, topping-up pump 8 is contained in side, stirred autoclave 13 upper end by support 7, attemperator comprises insulation can 14, insulation can 14 upper end is provided with water outlet 6, insulation can 14 times ends are provided with water-in, strumbox 1 is provided with multistorey strainer mesh 2.
Present configuration is novel, by the design of attemperator and topping-up pump, meet required temperature condition and pressure condition when reacting, accelerate speed of response, improve production efficiency, again by the design of stir shaft and paddle wheel, raw material is fully stirred when reacting, make it abundant reaction, then by the design of solid liquid centrifuge separator and strumbox so that after the reaction can by solid-liquid separator separation solid phase and liquid phase, purified further liquid phase by strumbox again, improve production efficiency, reduce production cost, meet production requirement.
To those skilled in the art, it is clear that the invention is not restricted to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit or the essential characteristic of the present invention, it is possible to realize the present invention in other specific forms. Therefore, no matter from which point, embodiment all should be regarded as exemplary, and right and wrong are restrictive, the scope of the present invention is limited by claims instead of above-mentioned explanation, it is intended that all changes in the implication of the equivalent important document dropping on claim and scope included in the present invention. Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, it is to be understood that, although this specification sheets is described according to enforcement mode, but not each enforcement mode only comprises an independent technical scheme, this kind of narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment through appropriately combined, can also form other enforcement modes that it will be appreciated by those skilled in the art that.
Claims (5)
1. a petrochemicals production unit, comprise stirred autoclave, it is characterized in that, described stirred autoclave is provided with stir shaft, described stir shaft is provided with paddle wheel, stir shaft upper end connects wheel box, described wheel box is equipped with motor, described stirred autoclave upper end is provided with opening for feed, side, described stirred autoclave upper end is provided with topping-up pump, outside described stirred autoclave, attemperator is housed, the lower end of described stirred autoclave is provided with discharge port, described stirred autoclave connects solid liquid centrifuge separator by discharge port, described solid liquid centrifuge separator upper end connects strumbox, the described solid lower end of liquid centrifuge separator is provided with solid phase discharging pipe, the lower end of described strumbox is provided with liquid phase discharging pipe.
2. a kind of petrochemicals production unit according to claim 1, it is characterised in that, described stirred autoclave upper end is provided with tensimeter.
3. a kind of petrochemicals production unit according to claim 1, it is characterised in that, described topping-up pump is contained in side, stirred autoclave upper end by support.
4. a kind of petrochemicals production unit according to claim 1, it is characterised in that, described attemperator comprises insulation can, and described insulation can upper end is provided with water outlet, and the lower end of described insulation can is provided with water-in.
5. a kind of petrochemicals production unit according to claim 1, it is characterised in that, described strumbox is provided with multistorey strainer mesh.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610145950.2A CN105617973A (en) | 2016-03-08 | 2016-03-08 | Petrochemical product production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610145950.2A CN105617973A (en) | 2016-03-08 | 2016-03-08 | Petrochemical product production equipment |
Publications (1)
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CN105617973A true CN105617973A (en) | 2016-06-01 |
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Family Applications (1)
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CN201610145950.2A Pending CN105617973A (en) | 2016-03-08 | 2016-03-08 | Petrochemical product production equipment |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108261999A (en) * | 2018-04-02 | 2018-07-10 | 胡琴 | A kind of petrochemical industry reaction kettle |
CN108295775A (en) * | 2017-12-25 | 2018-07-20 | 朱园园 | A kind of rate controlling type feeding device of solid-liquid reaction |
CN108479681A (en) * | 2018-04-02 | 2018-09-04 | 胡琴 | A kind of petrochemical industry method for producing |
CN111298749A (en) * | 2020-03-19 | 2020-06-19 | 中国热带农业科学院湛江实验站 | Bagasse cellulose and lignin centrifugal separation synchronous processing screening equipment |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202666832U (en) * | 2012-06-19 | 2013-01-16 | 东营市天正化工有限公司 | Solid-liquid separation filtering device |
CN204220139U (en) * | 2014-10-24 | 2015-03-25 | 天津晟高创新科技有限公司 | A kind of mixing and filtrating device preparing liquid cement grinding additive |
CN104707557A (en) * | 2015-02-09 | 2015-06-17 | 福建工程学院 | Method for preparing heavy metal adsorption material from waste circuit board non-metal powder |
CN205413012U (en) * | 2016-03-08 | 2016-08-03 | 何小平 | Petrochemical production equipment |
-
2016
- 2016-03-08 CN CN201610145950.2A patent/CN105617973A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202666832U (en) * | 2012-06-19 | 2013-01-16 | 东营市天正化工有限公司 | Solid-liquid separation filtering device |
CN204220139U (en) * | 2014-10-24 | 2015-03-25 | 天津晟高创新科技有限公司 | A kind of mixing and filtrating device preparing liquid cement grinding additive |
CN104707557A (en) * | 2015-02-09 | 2015-06-17 | 福建工程学院 | Method for preparing heavy metal adsorption material from waste circuit board non-metal powder |
CN205413012U (en) * | 2016-03-08 | 2016-08-03 | 何小平 | Petrochemical production equipment |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108295775A (en) * | 2017-12-25 | 2018-07-20 | 朱园园 | A kind of rate controlling type feeding device of solid-liquid reaction |
CN108261999A (en) * | 2018-04-02 | 2018-07-10 | 胡琴 | A kind of petrochemical industry reaction kettle |
CN108479681A (en) * | 2018-04-02 | 2018-09-04 | 胡琴 | A kind of petrochemical industry method for producing |
CN111298749A (en) * | 2020-03-19 | 2020-06-19 | 中国热带农业科学院湛江实验站 | Bagasse cellulose and lignin centrifugal separation synchronous processing screening equipment |
CN111298749B (en) * | 2020-03-19 | 2022-02-22 | 中国热带农业科学院湛江实验站 | Bagasse cellulose and lignin centrifugal separation synchronous processing screening equipment |
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Application publication date: 20160601 |
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