CN205627933U - White carbon black production reation kettle - Google Patents

White carbon black production reation kettle Download PDF

Info

Publication number
CN205627933U
CN205627933U CN201620259776.XU CN201620259776U CN205627933U CN 205627933 U CN205627933 U CN 205627933U CN 201620259776 U CN201620259776 U CN 201620259776U CN 205627933 U CN205627933 U CN 205627933U
Authority
CN
China
Prior art keywords
pipe
sulphuric acid
waterglass
discharger
kettle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620259776.XU
Other languages
Chinese (zh)
Inventor
陈君华
陈晨
郭雨
陈士夫
周丽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui University of Science and Technology
Original Assignee
Anhui University of Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Anhui University of Science and Technology filed Critical Anhui University of Science and Technology
Priority to CN201620259776.XU priority Critical patent/CN205627933U/en
Application granted granted Critical
Publication of CN205627933U publication Critical patent/CN205627933U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The utility model provides a white carbon black production reation kettle, including the cauldron body, be connected with water glass filling tube, sulphuric acid filling tube and steam heating pipe on the cauldron body, the reinforced Y -pipe of water glass, the reinforced Y -pipe of sulphuric acid are connected respectively to water glass filling tube, sulphuric acid filling tube, and water glass feed in raw material Y -pipe, the reinforced Y -pipe of sulphuric acid and is located the top that the cauldron was personally experienced sth. Part of the body, the reinforced Y -pipe of water glass has the reinforced branch pipe of three water glass, and a water glass discharger is connected respectively to the end of three reinforced branch pipes of water glass, the reinforced Y -pipe of sulphuric acid has the reinforced branch pipe of three sulphuric acid, and a sulphuric acid discharger is connected respectively to the end of three reinforced branch pipes of sulphuric acid, three water glass discharger and the alternate setting of three sulphuric acid discharger. The utility model discloses the raw materials adds degree of consistency height, under the circumstances of fast reaction, does benefit to control product granularity, can collect the surplus steam that steam heating produced and recycle, presss from both sides intraformational hot -water heating with the cauldron body, and the water after the heating can be personally experienced sth. Part of the body to the cauldron and kept warm and preheat, improves heat energy utilization efficiency simultaneously.

Description

A kind of white carbon black production reactor
Technical field
This utility model relates to commercial production reactor field, particularly relates to a kind of white carbon black production reactor.
Background technology
The broad understanding of reactor i.e. has the container physically or chemically reacted, by designing the structure of container With parameter configuration, it is achieved the heating of technological requirement, evaporate, cool down and the mixture function of low high speed.
Reactor is widely used in oil, chemical industry, rubber, pesticide, dyestuff, medicine, food, is used for Complete sulfuration, nitrification, hydrogenation, hydrocarbonylation, be polymerized, the pressure vessel of the technical process such as condensation, the most instead Answer device, reaction pot, decomposition pot, polymeric kettle etc.;Material typically has carbon manganese steel, rustless steel, zirconium, Ni-based (Kazakhstan, Monel, inconel) alloy and other composite.
For white carbon commercial production reactor, the raw material added in reactor is mainly waterglass and sulfur Acid, heats with steam.In existing dialogue carbon black industry production reactor raw material adding procedure, the uniformity is not Height, is unfavorable for that raw material reaction and product granularity control, and steam heating energy source utilization rate is low.
Utility model content
The purpose of this utility model is to provide a kind of white carbon black production reactor, asks solving above-mentioned technology Topic.
Technical problem to be solved in the utility model realizes by the following technical solutions:
A kind of white carbon black production reactor, it is characterised in that: including kettle, kettle connects waterglass Charge pipe, sulphuric acid charge pipe and steam-heating pipe, described waterglass charge pipe and sulphuric acid charge pipe are connected to The top of kettle, described steam-heating pipe is passed through the inner bottom part of kettle, described waterglass charge pipe, sulphuric acid Charge pipe connects waterglass charging Y-pipe, sulphuric acid charging Y-pipe, described waterglass charging trident respectively Pipe, sulphuric acid charging Y-pipe is positioned at the inner top of kettle;Described waterglass charging Y-pipe has San Tiaoshui Glass charging arm, the end of three waterglass charging arms connects a waterglass discharger respectively, and three Individual waterglass discharger uniform ring is located at kettle inner top;Described sulphuric acid charging Y-pipe has three sulphuric acid Charging arm, the end of three sulphuric acid charging arms connects a sulphuric acid discharger respectively, and three sulphuric acid go out Glassware uniform ring is located at kettle inner top;Three described waterglass dischargers and three sulphuric acid discharger phases Between arrange.
Described waterglass discharger and sulphuric acid discharger be uniformly arranged below with some discharging openings, described Waterglass discharger and sulphuric acid discharger are circular arc.
Being additionally provided with pH on-line monitoring sensor and temperature detection sensor in described kettle, described temperature is examined Survey sensor and constitute Temperature Feedback regulation with steam heating;PH on-line monitoring sensor can realize reactor The pH value real-time online detection of interior material.
Described kettle is made up of internal layer and outer layer, constitutes heat preservation sandwich layer, insulation between described internal layer and outer layer It is filled with deionized water in interlayer, is provided with steam mozzle in described heat preservation sandwich layer, under steam mozzle End inserts below deionized water liquid level, and steam mozzle upper end is connected to the top of internal layer, described outer layer Top is provided with remaining steam outlet, and the bottom of described outer layer is provided with deionized water floss hole.
Described steam mozzle lower end connects Y-pipe, makes steam discharge along different directions in heat preservation sandwich layer, Deionized water is heated.
Steam within kettle internal layer is derived from steam mozzle, is passed into below deionized water liquid level, right Deionized water heats, and steam unnecessary in interlayer is then discharged by remaining steam outlet.
Above-mentioned waterglass charging Y-pipe, sulphuric acid charging Y-pipe it be also possible to use four breeches pipes, five breeches pipes, six Breeches pipes etc. replace.
The outer surface parcel insulation material of kettle outer layer.
The beneficial effects of the utility model are:
This utility model raw material adds uniformity height, in the case of fast reaction, is beneficial to control product granularity, Steam can be added thermogenetic remaining steam and be collected recycling, the water in kettle interlayer be heated, heating After water kettle can be incubated and preheats, improve utilization efficiency of heat energy simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is waterglass charge pipe, the schematic top plan view of sulphuric acid charge pipe setting;
Fig. 3 is the discharging opening set-up mode of waterglass discharger.
Detailed description of the invention
For the technological means making this utility model realize, creation characteristic, reach purpose and be prone to bright with effect White understand, below in conjunction with specific embodiments and the drawings, this utility model be expanded on further, but following enforcement Example is only preferred embodiment of the present utility model, and not all.Based on the embodiment in embodiment, Those skilled in the art are obtained other embodiments on the premise of not making creative work, broadly falls into Protection scope of the present invention.
Specific embodiment of the utility model is described below in conjunction with the accompanying drawings.
As shown in Figure 1, Figure 2, Figure 3 shows, a kind of white carbon black production reactor, including kettle 2, kettle 2 connects Being connected to waterglass charge pipe 5, sulphuric acid charge pipe 4 and steam-heating pipe 1, waterglass charge pipe 5 and sulphuric acid add Material pipe 4 is connected to the top of kettle 2, and steam-heating pipe 1 is passed through the inner bottom part of kettle 2, waterglass charge pipe 5, Sulphuric acid charge pipe 4 connects waterglass charging Y-pipe 6, sulphuric acid charging Y-pipe 3, waterglass charging three respectively Breeches pipe 6, sulphuric acid charging Y-pipe 3 is positioned at the inner top of kettle 2;Waterglass charging Y-pipe 6 has three Waterglass charging arm 61, the end of three waterglass charging arms 61 connects a waterglass discharging respectively Device 62, three waterglass discharger 62 uniform ring are located at kettle 2 inner top;Sulphuric acid charging Y-pipe 3 has Article three, sulphuric acid charging arm 31, the end of three sulphuric acid charging arms 31 connects a sulphuric acid discharger respectively 32, three sulphuric acid discharger 32 uniform ring are located at kettle 2 inner top;Three waterglass dischargers 62 and three The alternate setting of sulphuric acid discharger 32;
Kettle 2 is made up of internal layer 21 and outer layer 22, constitutes heat preservation sandwich layer 9, protect between internal layer 21 and outer layer 22 It is filled with deionized water in temperature interlayer 9, in heat preservation sandwich layer 9, is provided with steam mozzle 8, steam mozzle 8 Below deionized water liquid level is inserted in lower end, and steam mozzle 8 upper end is connected to the top of internal layer 21, outer layer 22 Top be provided with remaining steam outlet 7, the bottom of outer layer 22 is provided with deionized water floss hole 10;
The top of kettle 2 be additionally provided with can the multipurpose charge door 11 of folding, the bottom of kettle 2 is provided with thing Material outlet 12.
In this utility model, " connection " can be fixing connection, it is also possible to is to removably connect, or It is integrally connected;Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, can be two The connection of element internal.For the ordinary skill in the art, can understand as the case may be Above-mentioned term concrete meaning in this utility model.
Of the present utility model ultimate principle, principal character and of the present utility model excellent have more than been shown and described Point.Skilled person will appreciate that of the industry, this utility model is not restricted to the described embodiments, above-mentioned Only preference of the present utility model described in embodiment and description, is not intended to limit this practicality new Type, on the premise of without departing from this utility model spirit and scope, this utility model also has various change And improvement, in the range of these changes and improvements both fall within claimed this utility model.This utility model Claimed scope is defined by appending claims and equivalent thereof.

Claims (4)

1. a white carbon black production reactor, it is characterised in that: including kettle, kettle connects water glass Glass charge pipe, sulphuric acid charge pipe and steam-heating pipe, described waterglass charge pipe and sulphuric acid charge pipe connect On the top of kettle, described steam-heating pipe is passed through the inner bottom part of kettle, described waterglass charge pipe, sulfur Acid charge pipe connects waterglass charging Y-pipe, sulphuric acid charging Y-pipe, described waterglass charging three respectively Breeches pipe, sulphuric acid charging Y-pipe is positioned at the inner top of kettle;Described waterglass charging Y-pipe has three Waterglass charging arm, the end of three waterglass charging arms connects a waterglass discharger respectively, Three waterglass discharger uniform ring are located at kettle inner top;Described sulphuric acid charging Y-pipe has three sulfur Acid charging arm, the end of three sulphuric acid charging arms connects a sulphuric acid discharger, three sulphuric acid respectively Discharger uniform ring is located at kettle inner top;Three described waterglass dischargers and three sulphuric acid dischargers Alternate setting.
White carbon black production reactor the most according to claim 1, it is characterised in that: described waterglass Discharger and sulphuric acid discharger be uniformly arranged below with some discharging openings, described waterglass discharger and sulfur Acid discharger is circular arc.
White carbon black production reactor the most according to claim 1, it is characterised in that: in described kettle also Being provided with pH on-line monitoring sensor and temperature detection sensor, described temperature detection sensor adds with steam Heat constitutes Temperature Feedback regulation.
White carbon black production reactor the most according to claim 1, it is characterised in that: described kettle is by interior Layer and outer layer constitute, between described internal layer and outer layer constitute heat preservation sandwich layer, be filled with in heat preservation sandwich layer from Sub-water, is provided with steam mozzle in described heat preservation sandwich layer, deionized water liquid is inserted in steam mozzle lower end Below face, steam mozzle upper end is connected to the top of internal layer, and the top of described outer layer is provided with remaining steam Outlet, the bottom of described outer layer is provided with deionized water floss hole.
CN201620259776.XU 2016-03-29 2016-03-29 White carbon black production reation kettle Expired - Fee Related CN205627933U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620259776.XU CN205627933U (en) 2016-03-29 2016-03-29 White carbon black production reation kettle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620259776.XU CN205627933U (en) 2016-03-29 2016-03-29 White carbon black production reation kettle

Publications (1)

Publication Number Publication Date
CN205627933U true CN205627933U (en) 2016-10-12

Family

ID=57066711

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620259776.XU Expired - Fee Related CN205627933U (en) 2016-03-29 2016-03-29 White carbon black production reation kettle

Country Status (1)

Country Link
CN (1) CN205627933U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108394911A (en) * 2018-05-28 2018-08-14 福建远翔新材料股份有限公司 A kind of white carbon reaction kettle means for feeding acid
CN108981163A (en) * 2018-07-09 2018-12-11 孟歆可 A kind of material heating device for integrating indirect heating and directly heating

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108394911A (en) * 2018-05-28 2018-08-14 福建远翔新材料股份有限公司 A kind of white carbon reaction kettle means for feeding acid
CN108981163A (en) * 2018-07-09 2018-12-11 孟歆可 A kind of material heating device for integrating indirect heating and directly heating
CN108981163B (en) * 2018-07-09 2021-08-06 浙江双浩软件开发有限公司 Material heating device integrating indirect heating and direct heating

Similar Documents

Publication Publication Date Title
CN201768561U (en) Graphite stirring kettle
CN205627933U (en) White carbon black production reation kettle
CN205435658U (en) Steam heating agitator tank
CN106882804A (en) The preparation method and preparation facilities of a kind of fluorographite
CN206995899U (en) A kind of energy-efficient distillation still
CN207483837U (en) Anti-soil film liquid plated film medicinal material automatic medicine adding apparatus
CN206055964U (en) Digital display three uses thermostatic water tank
CN201586522U (en) Horizontal continuous pressure leaching kettle for defluorinated lepidolite
CN206831832U (en) A kind of light hydrocarbon carburetors
CN206334557U (en) A kind of Cosmetic Manufacture material heater
CN208008770U (en) A kind of making vinegar gelatinization pot
CN208098082U (en) A kind of waterproofing agent production reaction kettle with temperature control system
CN207243820U (en) A kind of modified coal tar pitch flashes reaction kettle
CN206474154U (en) A kind of reactor for synthesizing bromohexane
CN206483170U (en) Malleation enrichment facility
CN205095767U (en) Jacket reaction kettle
CN206101508U (en) Soybean soaking jar
CN205323772U (en) Multifunctional reaction still
CN208356729U (en) A kind of feeding device for pre-add hydrogen
CN204380294U (en) For easily producing the distilling apparatus of corrosive gas
CN214390183U (en) Constant temperature reaction kettle
CN207237957U (en) A kind of steam condensate reuse means for aromatisation production
CN216972437U (en) Asphalt melting tank
CN202281205U (en) Water vapor generator
CN212523043U (en) Condensed milk concentration device

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

Granted publication date: 20161012

Termination date: 20170329

CF01 Termination of patent right due to non-payment of annual fee