CN205838896U - A kind of polystyrene process units installing condenser at vacuum blower entrance additional - Google Patents

A kind of polystyrene process units installing condenser at vacuum blower entrance additional Download PDF

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Publication number
CN205838896U
CN205838896U CN201620818046.9U CN201620818046U CN205838896U CN 205838896 U CN205838896 U CN 205838896U CN 201620818046 U CN201620818046 U CN 201620818046U CN 205838896 U CN205838896 U CN 205838896U
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CN
China
Prior art keywords
grades
collecting tank
devolatilizer
condenser
liquid collecting
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Active
Application number
CN201620818046.9U
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Chinese (zh)
Inventor
陈章华
苏杰
关杰华
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.)
Huizhou Benxin new material Limited by Share Ltd
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Huizhou Ren Hui Group Co Ltd
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Priority to CN201620818046.9U priority Critical patent/CN205838896U/en
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Abstract

The utility model discloses a kind of polystyrene process units installing condenser at vacuum blower entrance additional, it relates to technical field of chemical.Two grades of devolatilizer are connected with the first liquid collecting tank and two grades of devolatilizer condensers respectively, the lower end of two grades of devolatilizer condensers is connected with the first liquid collecting tank, first liquid collecting tank is connected with circulation ethylbenzene collecting tank, the upper end of two grades of devolatilizer condensers is connected with vacuum blower, vacuum blower is connected with the second liquid collecting tank and the first cycle condenser respectively, first cycle condenser is connected with the second cycle condenser and liquid-ring vacuum pump respectively, and the second cycle condenser is connected with liquid-ring vacuum pump.It can overcome the drawback of prior art, and novel in structural design is reasonable, and condenser is installed additional in the devolatilization gas outlet two grades of devolatilizer, and heavy component material condensation is recovered to liquid collecting tank.Heavy component material is effectively removed, and seldom returns to production system;The vacuum blower of two grades of devolatilizer is bled, and load is little, vacuum improves, internal temperature reduces and device fails is less.

Description

A kind of polystyrene process units installing condenser at vacuum blower entrance additional
Technical field:
This utility model relates to a kind of polystyrene process units installing condenser at vacuum blower entrance additional, belongs to chemical industry Equipment technical field.
Background technology:
The heavy component devolatilization of two grades of devolatilizer in polystyrene process units is natural cooling removal method at present, does not has There is condenser.There is following defect in this natural cooling removal method: 1, heavy component devolatilization weak effect, part heavy component material Production system can be returned to;2, the vacuum blower of two grades of devolatilizer is bled, and load is big, vacuum is low, internal temperature is high and equipment is easy Break down.3, two grades of devolatilizer heavy component removing workshop section heavy component material is not removed completely.
Utility model content:
For the problems referred to above, the technical problems to be solved in the utility model is to provide one and installs additional cold at vacuum blower entrance The polystyrene process units of condenser.
This utility model two takes off vacuum blower entrance and adds tube condenser, and it is cold that it comprises 1, two grades of devolatilizer of two grades of devolatilizer Condenser the 2, first liquid collecting tank 3, circulation ethylbenzene collecting tank 4, vacuum blower the 5, second liquid collecting tank the 6, first cycle condenser 7, second Cycle condenser 8 and liquid-ring vacuum pump 9, two grades of devolatilizer 1 are connected with the first liquid collecting tank 3 and two grades of devolatilizer condensers 2 respectively, The lower end of two grades of devolatilizer condensers 2 is connected with the first liquid collecting tank 3, and the first liquid collecting tank 3 is connected with circulation ethylbenzene collecting tank 4, and two Level devolatilizer condenser 2 upper end be connected with vacuum blower 5, vacuum blower 5 respectively with the second liquid collecting tank 6 and the first circulating condensing Device 7 connects, and the first cycle condenser 7 is connected with the second cycle condenser 8 and liquid-ring vacuum pump 9 respectively, and the second circulating condensing Device 8 is connected with liquid-ring vacuum pump 9.
The beneficial effects of the utility model: it can overcome the drawback of prior art, novel in structural design is reasonable, takes off at two grades Condenser is installed additional in the devolatilization gas outlet waving device, and heavy component material condensation is recovered to liquid collecting tank.Heavy component material obtains effectively Removing, seldom returns to production system;The vacuum blower of two grades of devolatilizer is bled, and load is little, vacuum improves, internal temperature reduces And device fails is less.
Accompanying drawing illustrates:
For ease of explanation, this utility model is embodied as and accompanying drawing is described in detail by following.
Fig. 1 is this utility model structural representation.
Detailed description of the invention:
As it is shown in figure 1, this detailed description of the invention is by the following technical solutions: it comprises 1, two grades of devolatilizer of two grades of devolatilizer Condenser the 2, first liquid collecting tank 3, circulation ethylbenzene collecting tank 4, vacuum blower the 5, second liquid collecting tank the 6, first cycle condenser 7, the Two cycle condensers 8 and liquid-ring vacuum pump 9, two grades of devolatilizer 1 connect with the first liquid collecting tank 3 and two grades of devolatilizer condensers 2 respectively Connecing, the lower end of two grades of devolatilizer condensers 2 is connected with the first liquid collecting tank 3, and the first liquid collecting tank 3 is connected with circulation ethylbenzene collecting tank 4, The upper end of two grades of devolatilizer condensers 2 is connected with vacuum blower 5, and vacuum blower 5 is cold with the second liquid collecting tank 6 and the first circulation respectively Condenser 7 connects, and the first cycle condenser 7 is connected with the second cycle condenser 8 and liquid-ring vacuum pump 9 respectively, and the second circulation is cold Condenser 8 is connected with liquid-ring vacuum pump 9.
Of the present utility model ultimate principle and principal character and of the present utility model advantage have more than been shown and described.One's own profession Skilled person will appreciate that of industry, this utility model is not restricted to the described embodiments, described in above-described embodiment and description Principle of the present utility model is simply described, on the premise of without departing from this utility model spirit and scope, this utility model is also Have various changes and modifications, 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 (1)

1. the polystyrene process units installing condenser at vacuum blower entrance additional, it is characterised in that: it comprises two grades and takes off Wave device (1), two grades of devolatilizer condensers (2), the first liquid collecting tank (3), circulation ethylbenzene collecting tank (4), vacuum blower (5), second Liquid collecting tank (6), the first cycle condenser (7), the second cycle condenser (8) and liquid-ring vacuum pump (9), two grades of devolatilizer (1) point It is not connected with the first liquid collecting tank (3) and two grades of devolatilizer condensers (2), the lower end of two grades of devolatilizer condensers (2) and the first collection Flow container (3) connect, the first liquid collecting tank (3) with circulation ethylbenzene collecting tank (4) be connected, the upper end of two grades of devolatilizer condensers (2) and Vacuum blower (5) connects, and vacuum blower (5) is connected with the second liquid collecting tank (6) and the first cycle condenser (7) respectively, and first follows Ring condenser (7) is connected with the second cycle condenser (8) and liquid-ring vacuum pump (9) respectively, and the second cycle condenser (8) and liquid Ring vacuum pump (9) connects.
CN201620818046.9U 2016-07-29 2016-07-29 A kind of polystyrene process units installing condenser at vacuum blower entrance additional Active CN205838896U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620818046.9U CN205838896U (en) 2016-07-29 2016-07-29 A kind of polystyrene process units installing condenser at vacuum blower entrance additional

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620818046.9U CN205838896U (en) 2016-07-29 2016-07-29 A kind of polystyrene process units installing condenser at vacuum blower entrance additional

Publications (1)

Publication Number Publication Date
CN205838896U true CN205838896U (en) 2016-12-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620818046.9U Active CN205838896U (en) 2016-07-29 2016-07-29 A kind of polystyrene process units installing condenser at vacuum blower entrance additional

Country Status (1)

Country Link
CN (1) CN205838896U (en)

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Address after: 516081 28 Petrochemical Road, Dayawan Petrochemical District, Huizhou, Guangdong.

Patentee after: Huizhou Benxin new material Limited by Share Ltd

Address before: 516081 28 Petrochemical Road, Dayawan Petrochemical District, Huizhou, Guangdong.

Patentee before: Huizhou Ren Hui Group Co., Ltd.