CN202490604U - Buffering storage liquid separating tank - Google Patents
Buffering storage liquid separating tank Download PDFInfo
- Publication number
- CN202490604U CN202490604U CN2012200796402U CN201220079640U CN202490604U CN 202490604 U CN202490604 U CN 202490604U CN 2012200796402 U CN2012200796402 U CN 2012200796402U CN 201220079640 U CN201220079640 U CN 201220079640U CN 202490604 U CN202490604 U CN 202490604U
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- tank body
- liquid level
- vacuum port
- material inlet
- tank
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Abstract
The utility model discloses a buffering storage liquid separating tank, which comprises a tank body, wherein the top of the tank body is respectively provided with a material inlet and a vacuum port connected with a reaction kettle or a condenser, and a pressure gage communicated with a tank cavity is installed on the tank body between the material inlet and the vacuum port; the side wall of the tank body is provided with a liquid level gage communicated with the tank body, and the bottom of the tank body is provided with a material outlet; the lower end of the material outlet is provided with a discharge pipe; and a discharge valve is arranged on the discharge pipe. The structural design of the buffering storage liquid separating tank is simple and reasonable. The vacuum port connected with the reaction kettle or the condenser and the material inlet are arranged on the tank body and are matched with the pressure gage, the liquid level gage and the discharge valve to form a circulation system, so that the utilization rate of materials is increased, the quality and the yield of products are increased, the environment is protected, and the energy is saved.
Description
Technical field:
The utility model relates to agitated reactor, relates in particular to a kind of buffering and stores the branch flow container.
Background technology:
In the technology the most commonly used, vacuum system directly connects with agitated reactor or condenser mutually, makes agitated reactor produce negative pressure, with the satisfied technological requirement that in still, adds liquid material material and the water of extracting the reaction generation out.In the process that vacuumizes reinforced and dehydration, inevitably extracted partial solvent and product out, caused raw material and product losses, reduced the yield and the quality of product, caused pollution to a certain degree.
Therefore, how in the process that adopts negative pressure feeding and dehydration, dealcoholysis etc. to operate, can not bring loss to raw material and product, the yield of product and quality and unaffected to the pollution of environment be problem demanding prompt solution.
The utility model content:
In order to remedy the defective of prior art, the purpose of the utility model provides a kind of buffering and stores the branch flow container, reasonable in design, and the utilization rate of material and the quality of product are improved.
The technical scheme of the utility model is following:
Buffering is stored and is divided flow container; Comprise tank body, it is characterized in that: described tank body top be respectively equipped with material inlet, with agitated reactor or the joining vacuum port of condenser, the Pressure gauge with jar chamber UNICOM is installed on the tank body between material inlet and the vacuum port; The sidewall of tank body is equipped with the liquid level gauge with tank body UNICOM; The bottom of tank body is provided with material outlet, and the material outlet lower end is equipped with vomit pipe, and vomit pipe is provided with baiting valve.
Described buffering is stored and is divided flow container, and it is characterized in that: described liquid level is counted glass tube formula liquid level gauge.
The utility model has the advantages that:
The utility model structural design advantages of simple; Cooperate Pressure gauge, liquid level gauge, baiting valve to constitute the circulatory system through on tank body, being provided with agitated reactor or the joining vacuum port of condenser and material mouth; Improved utilization of materials, the quality and the yield of product get a promotion environmental protection and energy saving.
Description of drawings:
Fig. 1 is the structural representation of the utility model.
The specific embodiment:
Referring to Fig. 1:
Buffering store to be divided a flow container, comprises tank body 1, tank body 1 top be respectively equipped with material inlet 2, with agitated reactor or the joining vacuum port 3 of condenser; Be equipped with on the tank body 1 between material inlet 2 and the vacuum port 3 and jar Pressure gauge 4 of chamber UNICOM; The sidewall of tank body 1 is equipped with the liquid level gauge 5 with tank body 1 UNICOM, and liquid level gauge 5 adopts glass tubular type liquid level gauge, and the bottom of tank body 1 is provided with material outlet 6; Material outlet 6 lower ends are equipped with vomit pipe 7, and vomit pipe 7 is provided with baiting valve 8.
What adopt in the actual process of the utility model is the stainless steel basin of 400 liters.Its operation principle: be that vavuum pump passes through vacuum orifice, in tank body 1, produce negative pressure, vacuum port connects with agitated reactor or condenser mutually.The reading of Pressure gauge indication is that the pressure in the tank body 1 (is about 0.083-0.095Mpa).Because the reactant in the still reacts under 90 ~ 140 ℃; In the operating process that vacuumizes; There are the solvent of a spot of product, part and the water of reaction generation to be drawn out of, temporarily are stored in this jar, can see that from glass tube level meter 5 liquid level is increasingly high; Approximately through the production of 30 batch products, liquid level can reach 2/3.Through leaving standstill, from the glass tube level meter, can clearly observe the stratification state of jar interior water and solvent, few products.Collect waste water through baiting valve 8, carry out recycling to solvent and product, produce certain economic benefits, avoided environmental pollution.
Claims (2)
1. a buffering is stored and is divided flow container; Comprise tank body, it is characterized in that: described tank body top be respectively equipped with material inlet, with agitated reactor or the joining vacuum port of condenser, the Pressure gauge with jar chamber UNICOM is installed on the tank body between material inlet and the vacuum port; The sidewall of tank body is equipped with the liquid level gauge with tank body UNICOM; The bottom of tank body is provided with material outlet, and the material outlet lower end is equipped with vomit pipe, and vomit pipe is provided with baiting valve.
2. buffering according to claim 1 is stored and is divided flow container, and it is characterized in that: described liquid level is counted glass tube formula liquid level gauge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200796402U CN202490604U (en) | 2012-03-05 | 2012-03-05 | Buffering storage liquid separating tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200796402U CN202490604U (en) | 2012-03-05 | 2012-03-05 | Buffering storage liquid separating tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202490604U true CN202490604U (en) | 2012-10-17 |
Family
ID=46996848
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200796402U Expired - Fee Related CN202490604U (en) | 2012-03-05 | 2012-03-05 | Buffering storage liquid separating tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202490604U (en) |
-
2012
- 2012-03-05 CN CN2012200796402U patent/CN202490604U/en not_active Expired - Fee Related
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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: 20121017 Termination date: 20180305 |