CN204768730U - Totally enclosed high temperature printing ink reation kettle - Google Patents

Totally enclosed high temperature printing ink reation kettle Download PDF

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Publication number
CN204768730U
CN204768730U CN201520586265.4U CN201520586265U CN204768730U CN 204768730 U CN204768730 U CN 204768730U CN 201520586265 U CN201520586265 U CN 201520586265U CN 204768730 U CN204768730 U CN 204768730U
Authority
CN
China
Prior art keywords
chemicals
reactor
mixing chamber
adding set
interpolation
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
CN201520586265.4U
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Chinese (zh)
Inventor
马永利
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.)
Tianjin Anguang Printing Ink Factory
Original Assignee
Tianjin Anguang Printing Ink Factory
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 Tianjin Anguang Printing Ink Factory filed Critical Tianjin Anguang Printing Ink Factory
Priority to CN201520586265.4U priority Critical patent/CN204768730U/en
Application granted granted Critical
Publication of CN204768730U publication Critical patent/CN204768730U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model belongs to the technical field of the printing ink processing equipment, especially, relate to a totally enclosed high temperature printing ink reation kettle, add device, chemicals mixing chamber, exhaust processing apparatus, reation kettle, agitating unit, level sensor, filter, storage device, motor -driven pump, can, stirring heating device, surge chamber, induction pipe, second chemicals interpolation device including first chemicals. The utility model discloses whole process need not artifical the interpolation, just can realize the interpolation of chemical reagent and raw materials through control valve, motor -driven pump, improves the work efficiency of system greatly, reduces labour cost, and it controls the accuracy, and reaction effect is good.

Description

A kind of Omniseal high-temperature ink reactor
Technical field
The utility model belongs to ink technical field of processing equipment, particularly relates to a kind of Omniseal high-temperature ink reactor.
Background technology
In Printing ink producing process, reactor is one of instrument of its indispensability, the effect of reactor pours in reactor by raw material and chemicals mixing material, then in still, places a period of time under specific isoperibol and carry out chemical reaction, the liquid needed for generation; Existing reactor only has the function making course of reaction be in steady temperature, raw material and chemicals mixing material need manually to add, this mode not only efficiency comparison is low, and owing to being added to the liquid level of the mixing material in reactor, can not higher than the position of reactor setting, otherwise cannot complete reaction, the liquid of output is defective; Lower than the liquid level line of setting, can not will reduce the amount that each reactor can produce liquid so simultaneously; For artificial interpolation, this controls to be difficult to hold.
Summary of the invention
The utility model provides a kind of Omniseal high-temperature ink reactor, to solve artificial interpolation traditional in above-mentioned background technology, inefficient problem.
The technical problem that the utility model solves realizes by the following technical solutions: the utility model provides a kind of Omniseal high-temperature ink reactor, it is characterized in that: comprise the first chemicals adding set, chemicals mixing chamber, exhaust gas treatment device, reactor, agitating device, liquid level sensor, filter, storage device, electrodynamic pump, can, agitating heater, surge chamber, ingress pipe, second chemicals adding set, the arranged outside can of described reactor, described exhaust gas treatment device is arranged on the upper side of reactor, described agitating device is arranged on the inside of reactor, described agitating heater is arranged on the top of reactor, and below is connected with agitating device, described surge chamber is arranged on the top of agitating heater, described chemicals mixing chamber is arranged on the top of surge chamber, and top is connected with electrodynamic pump by ingress pipe, described first chemicals adding set is arranged on the side of chemicals mixing chamber, described second chemicals adding set is arranged on the opposite side of chemicals mixing chamber, described liquid level sensor is arranged on the inwall of reactor, and described filter is connected with the bottom of reactor, and described storage device is connected with filter.
Between described first chemicals adding set and chemicals mixing chamber, control valve is installed.
Between described second chemicals adding set and chemicals mixing chamber, control valve is installed.
The top of described chemicals mixing chamber is provided with seal cover.
The beneficial effects of the utility model are:
1, raw material is incorporated into reactor by electrodynamic pump by the utility model, then chemical reagent is added respectively in the first chemicals adding set and the second chemicals adding set, fully mix in chemicals mixing chamber, enter in reactor and raw material reaction through surge chamber, then agitating heater heats to agitating device, agitating device realizes adding thermal agitation at reactor, chemical mixtures and raw material are fully reacted, filtered by filter after reaction, finally stored by storage device, whole process is without the need to artificial interpolation, by control and regulation valve, electrodynamic pump just can realize the interpolation of chemical reagent and raw material, greatly improve the operating efficiency of system, reduce labour cost, it controls accurately, reaction effect is good.
2, the utility model adopts can and agitating heater, to realizing sealing hot environment in reactor, chemical reagent and raw material is fully reacted, and avoids raw material reaction incomplete, and the underproof situation of liquid of output occurs.
3, the utility model adopts the design of liquid level sensor, the liquid level of the mixing material be added in reactor can be detected at any time, be convenient to timely interpolation, make the position that the liquid level of mixing material can not set higher than reactor, reach the environment of fully reaction, improve the qualification rate of the liquid of output.
4, the utility model adopts the design of exhaust gas treatment device, is processed by Exhaust Gas, avoids discharging its direct exhaust emission environment.
5, the utility model structure is simple, and each parts are relatively more cheap, low cost of manufacture.
Accompanying drawing explanation
Fig. 1 is structure chart of the present utility model.
Detailed description of the invention
In figure: 1-first chemicals adding set, 2-chemicals mixing chamber, 3-exhaust gas treatment device, 4-reactor, 5-agitating device, 6-liquid level sensor, 7-filter, 8-storage device, 9-electrodynamic pump, 10-can, 11-agitating heater, 12-surge chamber, 13-ingress pipe, 14-second chemicals adding set, 15-control valve.
Below in conjunction with accompanying drawing, the utility model is described further:
Embodiment:
As shown in Figure 1, the present embodiment comprises: the first chemicals adding set 1, chemicals mixing chamber 2, exhaust gas treatment device 3, reactor 4, agitating device 5, liquid level sensor 6, filter 7, storage device 8, electrodynamic pump 9, can 10, agitating heater 11, surge chamber 12, ingress pipe 13, second chemicals adding set 14, the arranged outside can 10 of described reactor 4, described exhaust gas treatment device 3 is arranged on the upper side of reactor 4, described agitating device 5 is arranged on the inside of reactor 4, described agitating heater 11 is arranged on the top of reactor 4, and below is connected with agitating device 5, described surge chamber 12 is arranged on the top of agitating heater 11, described chemicals mixing chamber 2 is arranged on the top of surge chamber 12, and top is connected with electrodynamic pump 9 by ingress pipe 13, described first chemicals adding set 1 is arranged on the side of chemicals mixing chamber 2, described second chemicals adding set 14 is arranged on the opposite side of chemicals mixing chamber 2, described liquid level sensor 6 is arranged on the inwall of reactor 4, described filter 7 is connected with the bottom of reactor 4, described storage device 8 is connected with filter 7.
Between described first chemicals adding set 1 and chemicals mixing chamber 2, control valve 15 is installed.
Between described second chemicals adding set 14 and chemicals mixing chamber 2, control valve 15 is installed.
The top of described chemicals mixing chamber 2 is provided with seal cover.
Raw material is incorporated into reactor by electrodynamic pump by the utility model, then chemical reagent is added respectively in the first chemicals adding set and the second chemicals adding set, fully mix in chemicals mixing chamber, enter in reactor and raw material reaction through surge chamber, then agitating heater heats to agitating device, agitating device realizes adding thermal agitation at reactor, chemical mixtures and raw material are fully reacted, filtered by filter after reaction, finally stored by storage device, whole process is without the need to artificial interpolation, by control and regulation valve, electrodynamic pump just can realize the interpolation of chemical reagent and raw material, greatly improve the operating efficiency of system, reduce labour cost, it controls accurately, reaction effect is good, adopting can and agitating heater, to realizing sealing hot environment in reactor, chemical reagent and raw material fully being reacted, avoid raw material reaction incomplete, the underproof situation of liquid of output occurs, adopt the design of liquid level sensor, the liquid level of the mixing material be added in reactor can be detected at any time, be convenient to timely interpolation, make the position that the liquid level of mixing material can not set higher than reactor, reach the environment of fully reaction, improve the qualification rate of the liquid of output, adopt the design of exhaust gas treatment device, Exhaust Gas is processed, avoids discharging its direct exhaust emission environment, structure is simple, and each parts are relatively more cheap, low cost of manufacture.
Utilize technical scheme described in the utility model, or those skilled in the art being under the inspiration of technical solutions of the utility model, designing similar technical scheme, and reach above-mentioned technique effect, is all fall into protection domain of the present utility model.

Claims (4)

1. an Omniseal high-temperature ink reactor, is characterized in that: comprise the first chemicals adding set, chemicals mixing chamber, exhaust gas treatment device, reactor, agitating device, liquid level sensor, filter, storage device, electrodynamic pump, can, agitating heater, surge chamber, ingress pipe, second chemicals adding set, the arranged outside can of described reactor, described exhaust gas treatment device is arranged on the upper side of reactor, described agitating device is arranged on the inside of reactor, described agitating heater is arranged on the top of reactor, and below is connected with agitating device, described surge chamber is arranged on the top of agitating heater, described chemicals mixing chamber is arranged on the top of surge chamber, and top is connected with electrodynamic pump by ingress pipe, described first chemicals adding set is arranged on the side of chemicals mixing chamber, described second chemicals adding set is arranged on the opposite side of chemicals mixing chamber, described liquid level sensor is arranged on the inwall of reactor, and described filter is connected with the bottom of reactor, and described storage device is connected with filter.
2. a kind of Omniseal high-temperature ink reactor according to claim 1, is characterized in that: install control valve between described first chemicals adding set and chemicals mixing chamber.
3. a kind of Omniseal high-temperature ink reactor according to claim 1, is characterized in that: install control valve between described second chemicals adding set and chemicals mixing chamber.
4. a kind of Omniseal high-temperature ink reactor according to claim 1, is characterized in that: the top of described chemicals mixing chamber is provided with seal cover.
CN201520586265.4U 2015-08-05 2015-08-05 Totally enclosed high temperature printing ink reation kettle Expired - Fee Related CN204768730U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520586265.4U CN204768730U (en) 2015-08-05 2015-08-05 Totally enclosed high temperature printing ink reation kettle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520586265.4U CN204768730U (en) 2015-08-05 2015-08-05 Totally enclosed high temperature printing ink reation kettle

Publications (1)

Publication Number Publication Date
CN204768730U true CN204768730U (en) 2015-11-18

Family

ID=54508861

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520586265.4U Expired - Fee Related CN204768730U (en) 2015-08-05 2015-08-05 Totally enclosed high temperature printing ink reation kettle

Country Status (1)

Country Link
CN (1) CN204768730U (en)

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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: 20151118

Termination date: 20180805