CN202968163U - Injection water preparation device capable of on-line sterilization of raw material water tank - Google Patents

Injection water preparation device capable of on-line sterilization of raw material water tank Download PDF

Info

Publication number
CN202968163U
CN202968163U CN 201220259585 CN201220259585U CN202968163U CN 202968163 U CN202968163 U CN 202968163U CN 201220259585 CN201220259585 CN 201220259585 CN 201220259585 U CN201220259585 U CN 201220259585U CN 202968163 U CN202968163 U CN 202968163U
Authority
CN
China
Prior art keywords
raw material
water
water tank
material water
condenser
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 - Lifetime
Application number
CN 201220259585
Other languages
Chinese (zh)
Inventor
叶湘武
余渊
冯世明
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.)
GUIZHOU JINGFENG INJECTION CO Ltd
Original Assignee
GUIZHOU JINGFENG INJECTION CO Ltd
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 GUIZHOU JINGFENG INJECTION CO Ltd filed Critical GUIZHOU JINGFENG INJECTION CO Ltd
Priority to CN 201220259585 priority Critical patent/CN202968163U/en
Application granted granted Critical
Publication of CN202968163U publication Critical patent/CN202968163U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model discloses an injection water preparation device capable of on-line sterilization of a raw material water tank. The device comprises the raw material water tank, a raw material water condenser, a cooling water condenser, an evaporation tower and a plurality of steam-water separation towers, wherein the tube pass inlet of the raw material water condenser is connected with the outlet of the raw material water tank. The device is characterized by further comprising a pre-heater, wherein the tube pass inlet of the pre-heater is connected with the tube pass outlet of the raw material water condenser, the tube pass outlet of the pre-heater is divided into two paths, one path is connected with the purified water inlet of the evaporation tower, the other path is connected with the raw material water tank, and industrial steam passes through a shell pass of the pre-heater. By adopting the injection water preparation device disclosed by the utility model, the problems existing in off-line sterilization or chemical sterilization of the raw material water tank in the pharmaceutical injection water preparation device are conquered, and the injection water preparation device is free from residue, free from mounting pollution, capable of on-line sterilization, convenient in operation and strong in operability.

Description

A kind ofly can carry out to the raw material water tank water for injection preparation facilities of online sterilization
Technical field:
The utility model relates to a kind of pharmaceutical purpose water for injection preparation facilities, particularly a kind ofly can carry out to the raw material water tank water for injection preparation facilities of online sterilization.
Background technology:
Referring to Fig. 1, existing water for injection preparation facilities comprises raw material water tank 1, raw water condenser 2, cooling water condensation device 3 and sextuple-effect evaporation tower 4,5,6,7,8,9, purified water in raw material water tank 1 pumps into the interior tube side of raw water condenser 2 by pump 10, with do not imitate preliminary heating after the pure steam heat exchange that evaporator tower 9 brings, send into again the tube side of the first effect evaporator tower 4, purified water enters the first effect evaporator tower 4 and accepts the heat of the outer high-temperature steam of tube wall and change pure steam into, and the first effect evaporator tower 4 shell side steam cooling levels are discharged simultaneously.After entering the purified water evaporation in the first effect evaporator tower 4, the pure gas of generation enters the second effect evaporator tower 5 shell sides as the heating source of the second effect evaporator tower 5, a part of purified water in the first effect evaporator tower 4 enter that the second effect evaporator tower 5 tube sides are inner continues evaporation, and other respectively imitates evaporator tower 6,7,8,9 working process.Each imitates evaporator tower 5,6,7,8,9 equivalent distilled water enter cooling water condensation device 3 and are condensed into 98 ℃ of left and right after raw water condenser 2 converges, in the shell side of the incoming stock water condenser 2 of pure steam that end effect evaporator tower 9 produces, purified water in raw water condenser 2 tube sides is carried out preheating, then enter water of condensation condenser 3 and be condensed into water for injection.
Above-mentioned existing water for injection preparation facilities exists a problem can't sterilize to the raw material water tank online exactly, can only use off-line or chemosterilization.
The utility model content:
Technical problem to be solved in the utility model is to provide a kind of water for injection preparation facilities of online sterilization that can carry out the raw material water tank for the existing existing problem of water for injection preparation facilities; It has overcome the sterilization of " raw material water tank " off-line in pharmaceutical purpose water for injection preparation facilities or the existing problem of chemosterilization, and this water for injection preparation facilities noresidue is polluted without installing, and online sterilization is easy to operate, strong operability.
Technical problem to be solved in the utility model can be achieved through the following technical solutions:
A kind ofly can carry out to the raw material water tank water for injection preparation facilities of online sterilization, comprise raw material water tank, raw water condenser, cooling water condensation device and an evaporator tower and several carbonated drink knockout towers, the tube side import of described raw water condenser is connected with the outlet of described raw material water tank, it is characterized in that, also comprise a preheater, the tube side entrance of described preheater is connected with the outlet of the tube side of described raw water condenser, two-way is told in the tube side outlet of preheater, one the tunnel is connected with the purified water entrance of described evaporator tower, and another road connects the raw material water tank; Walk industrial steam in the shell side of described preheater.
Principle of work of the present utility model is: the purified water in the raw material water tank pumps into tube side in the raw water condenser by pump, with do not imitate preliminary heating after the pure steam heat exchange that evaporator tower brings, then enter in the tube side of preheater, the industrial steam that is preheated in the device shell side is heated to 121 ℃, be heated to 121 ℃ of one tunnel tube side of sending into the first effect evaporator tower interior by the outer industrial steam continuation heating of tube wall, another road is controlled by valve and is sent into the raw material water tank, and the raw material water tank is sterilized online.Purified water enters the first effect evaporator tower and accepts the heat of the outer high-temperature steam of tube wall and change pure steam into, and the first effect evaporator tower shell side steam cooling level is discharged simultaneously.After entering the purified water evaporation in the first effect evaporator tower, the pure gas of generation enters the second effect evaporator tower shell side as the heating source of the second effect evaporator tower, the a part of purified water of the first effect in evaporator tower enter that the second effect evaporator tower tube side is inner continues evaporation, and other respectively imitates the evaporator tower working process.Each is imitated evaporator tower equivalence distilled water and enters the cooling water condensation device be condensed into 98 ℃ of left and right after the raw water condenser converges, in the shell side of the incoming stock water condenser of pure steam that the end effect evaporator tower produces, purified water in raw water condenser tube side is carried out preheating, then enter the water of condensation condenser condenses and become water for injection.
The utility model has overcome the sterilization of " raw material water tank " off-line in pharmaceutical purpose water for injection preparation facilities or the existing problem of chemosterilization, and this water for injection preparation facilities noresidue is polluted without installing, and online sterilization is easy to operate, strong operability.
Description of drawings
Fig. 1 is the structural representation of existing water for injection preparation facilities.
Fig. 2 is the structural representation of the utility model water for injection preparation facilities.
Embodiment
Further describe the utility model below in conjunction with the drawings and specific embodiments.
Referring to Fig. 2, what provide in figure a kind ofly can carry out the water for injection preparation facilities of online sterilization to the raw material water tank, comprise raw material water tank 1, raw water condenser 2, cooling water condensation device 3, preheater 11 and sextuple-effect evaporation tower 4,5,6,7,8,9.
The outlet of raw material water tank 1 is connected with the tube side import of raw water condenser 2 by pump 10 and pipeline, the tube side outlet of raw water condenser 2 is connected with the tube side entrance of preheater 11 by pipeline, two-way is told in the tube side outlet of preheater 11, the valve 12 of leading up to is connected with the purified water entrance of pipeline with the first effect evaporator tower 4, and another road connects raw material water tank 1 by valve 13 and pipeline; Walk industrial steam in the shell side of preheater 11.
Purified water in raw material water tank 1 pumps into the interior tube side of raw water condenser 2 by pump 10, with do not imitate preliminary heating after the pure steam heat exchange that evaporator tower 9 brings, then enter in the tube side of preheater 11, the industrial steam that is preheated in device 11 shell sides is heated to 121 ℃, be heated to 121 ℃ of one tunnel tube side of sending into the first effect evaporator tower 4 interior by the outer industrial steam continuation heating of tube wall, another road is controlled by valve 13 and is sent into raw material water tank 1, and raw material water tank 1 is sterilized online.
Purified water enters the first effect evaporator tower 4 and accepts the heat of the outer high-temperature steam of tube wall and change pure steam into, and the first effect evaporator tower 4 shell side steam cooling levels are discharged simultaneously.After entering the purified water evaporation in the first effect evaporator tower 4, the pure gas of generation enters the second effect evaporator tower 5 shell sides as the heating source of the second effect evaporator tower 5, a part of purified water in the first effect evaporator tower 4 enter that the second effect evaporator tower 5 tube sides are inner continues evaporation, and other respectively imitates evaporator tower 6,7,8,9 working process.Each imitates evaporator tower 5,6,7,8,9 equivalent distilled water enter cooling water condensation device 3 and are condensed into 98 ℃ of left and right after raw water condenser 2 converges, in the shell side of the incoming stock water condenser 2 of pure steam that end effect evaporator tower 9 produces, purified water in raw water condenser 2 tube sides is carried out preheating, then enter water of condensation condenser 3 and be condensed into water for injection.

Claims (1)

1. one kind can be carried out to the raw material water tank water for injection preparation facilities of online sterilization, comprise raw material water tank, raw water condenser, cooling water condensation device and an evaporator tower and several carbonated drink knockout towers, the tube side import of described raw water condenser is connected with the outlet of described raw material water tank, it is characterized in that, also comprise a preheater, the tube side entrance of described preheater is connected with the outlet of the tube side of described raw water condenser, two-way is told in the tube side outlet of preheater, one the tunnel is connected with the purified water entrance of described evaporator tower, and another road connects the raw material water tank; Walk industrial steam in the shell side of described preheater.
CN 201220259585 2012-06-04 2012-06-04 Injection water preparation device capable of on-line sterilization of raw material water tank Expired - Lifetime CN202968163U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220259585 CN202968163U (en) 2012-06-04 2012-06-04 Injection water preparation device capable of on-line sterilization of raw material water tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220259585 CN202968163U (en) 2012-06-04 2012-06-04 Injection water preparation device capable of on-line sterilization of raw material water tank

Publications (1)

Publication Number Publication Date
CN202968163U true CN202968163U (en) 2013-06-05

Family

ID=48509266

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220259585 Expired - Lifetime CN202968163U (en) 2012-06-04 2012-06-04 Injection water preparation device capable of on-line sterilization of raw material water tank

Country Status (1)

Country Link
CN (1) CN202968163U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106186497A (en) * 2016-08-31 2016-12-07 淄博华周制药设备有限公司 Purified water, distilled water, pure steam all-in-one
CN107963681A (en) * 2017-10-18 2018-04-27 楚天华通医药设备有限公司 A kind of multistage steam recompresses formula distillation machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106186497A (en) * 2016-08-31 2016-12-07 淄博华周制药设备有限公司 Purified water, distilled water, pure steam all-in-one
CN106186497B (en) * 2016-08-31 2023-05-23 淄博华周制药设备有限公司 Purified water, distilled water and pure steam all-in-one machine
CN107963681A (en) * 2017-10-18 2018-04-27 楚天华通医药设备有限公司 A kind of multistage steam recompresses formula distillation machine

Similar Documents

Publication Publication Date Title
CN105366867B (en) A kind of single-action multicell mechanical compress evaporation process high salt/high organic wastewater device and method
CN107324426A (en) A kind of residual heat from boiler fume coupling evaporation concentrates desulfurization wastewater system
CN105036223A (en) High-efficiency energy-saving sewage treatment method and device
CN102249472A (en) Adsorption compression-multiple-effect distillation system
CN202968163U (en) Injection water preparation device capable of on-line sterilization of raw material water tank
CN203700098U (en) Device for treating power plant waste water with steam waste heat of thermal power plant
CN103394203A (en) Technology for preparing injection water through low temperature multi-effect distillation and system for implementing technology
CN204404134U (en) Pure steam generator
CN206680208U (en) A kind of residual heat from boiler fume coupling evaporation concentrates desulfurization wastewater system
CN102527070A (en) Free energy heat pump multiple-effect evaporation device and process
CN105588108A (en) System for replenishing water to steam boiler by means of steam condensate
CN202087068U (en) Energy-saving liquid ammonia evaporating device
CN202116342U (en) Industrial exhaust heat low-temperature multiple-effect seawater desalinization system
CN101525196A (en) Multi-effect distilled seawater desalting plant with pre-heater
CN203281053U (en) Quadruple-effect downstream falling-film evaporator for preparation of inositol
CN205442935U (en) Concentrated processing system of waste lye
CN204873907U (en) Hot pressing formula distilled water machine system
CN204778912U (en) Concentrated processing system of evaporation formula liquid
CN205261506U (en) Steam circulation system of health preserving wine extraction element
CN204824241U (en) Sewage treatment system
CN204159044U (en) The cold tank of a kind of sudden strain of a muscle with vapor-recovery system
CN209098231U (en) A kind of low temperature multiple-effect distillation sea water desalting device
CN204134242U (en) A kind of Calcium Chloride Production special evaporator
CN106219650A (en) A kind of low-quality bootstrap system of steel plant and using method thereof
CN205653193U (en) Concentrated system of waste water vacuum flashing

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20130605