Energy recovery pump in reverse osmosis desalination plants

Energy recovery pump in reverse osmosis desalination plants

Desdination, 54(1985)117-126 117 Elsevier Science Publishers B.V.,Amsterdam-PrintedinThe Netherlands ENERGY RECOVERY PUMPS IN REVERSE OSMOSIS DESAL...

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Desdination, 54(1985)117-126

117

Elsevier Science Publishers B.V.,Amsterdam-PrintedinThe Netherlands

ENERGY RECOVERY PUMPS IN REVERSE OSMOSIS DESALINATION PLANTS P. Goubeau, Pompes Guinard, 45, Av. du Pont, De Tasset, 74000 Annecy, France

INTRODUCTION

I.

With the fresh water supply critically low in many places, and with the quality and availability of fresh water decreasing, desalination is a vital solution to this major problem. Of the many desalting processes existing today, reverse osmosis (R/O) is growing fast, and although it is still being developed and improved, it is already a leading method of desalination. The reason for this is that R/O meets two of the most important requirements for desalination: low running cost and low energy consumption. These advantages of reverse osmosis can be further improved by using an energy recovery device. There are several ways of reducing running cost and energy consumption, and the choice of the right one is very important. There is now enough experience in the different aspects of energy recovery to allow comparison of the different systems. The following presentation will include, after a quick review of desalination requirements, a description of the integrated energy recovery pumping system and a comparison of the two major technologieswhich take advantage of the remaining energy of the concentrated brine of the R/O process.

II.

THE REQUIREMENTS OF DESALINATION BY REVERSE OSMOSIS

1) Desalination of sea water Desalination is a vital problem for the user countries. The local activity, whether it is industry or tourism, very often relies on the fresh water supply. Thus, the first priority is to produce fresh water reliably. The second point is that these plants are generally in very remote areas, so maintenance should be as infrequent and as simple as possible. Lastly, the users, except in the Middle East, generally have high energy costs. 2)

Advantages of reverse osmosis vs thermal process:

Lower running costs (especially energy consumption), shorter delivery time and some technical aspects like low temperature, and all the energy being in tha. form of pressure. In reverse osmosis, three main points have to be considered: a) salted water pretreatment: This problem is now well known and many companies have good experience in this matter. Improper pretreatment can

118 shorten the life of the membranes and reduce the quality of the produced fresh water. b) Membranes: There are several different kinds of membranes on the market now, some of which are new, and others which have been in use for a long time. The result of membrane failure is poor fresh water quality and membrane replacement costs. c) The high pressure pumping or energy recovery pumping system: The result of failure is non-production. Thus it is vital for the customers, consultants and contractors to choose the most suitable equipment for the high pressure pumping system. 3)

Requirements for reverse osmosis plant equipment

In the view to save, even to improve the advantages of the reverse osmosis vs thermal processes, all the equipment has to meet the following requirements Producing water "any way": high reliability.

: low maintenance

Low running cost

low energy consumption. Flexibility to adapt to the needs of the users, including winter-summer (intake water temperaturevariations) long term : especially for brackish water because of TDS variation and generally because of modification of the membrane characteristics, Possibility of modification to meet new data (as the pumping equipment is generally designed for a 20 years running time, one can expect that new membranes will be available by this time, and the pumping equipment should meet the new data requirements with as few modifications as possible.) Simple running procedure and regulation. Short deliveries.

REVERSE OSMOSIS DESALINATION

REQUIREMENTS

LOWRUNNING

,

HIGH EFFICIENCY LOW MAINTENANCE

FLEXISILITY

>

HYDRAULIC

DESIGN

LONG RANGE FLEXIBILITY

>

EVOLUTING

DESIGN

RELIABILITY

_ ..___

COST

ANSWERS

*

DESIGN CRITERIA

----.-

119 III. THE ENERGY RECOVERY PUMPING SYSTEMS There are two ways to meet the requirements of the reverse osmosis process: 1) to use standard water or petroleum pumping equipment for this particular application. 2) to design and develop a complete system exactly adapted to this application. Our experience in

standard energy recovery pumping system (we have

been supplying energy recovery equipments for petro-chemical industry for the past 20 years) showed that this standard systems may not be well adapted to all sizes of R/O plants, especially regarding cost, maintenance and flexibility. Then, POMPES GUINARD decided to put its experience in the service of the development of an adapted energy recovery pumping system, known under the name of "TPMDX".

INTEGRATED SYSTEM T?MDX

PUMP + TURBINE

SEPARATED UNITS

THE ENERGY

RECOVERY

PUMPING SYSTEMS

For that POMPES GUINARD used: 1)

Its nuclear experience for safety and reliability

Medium high speed (4000 to 9000 RMP) Oil lubrication systems Type of bearing (tilting pad oil lubrication or hydrostatic bearings). This experience is the result of

25

years

of development and technical impro-

vement, proven by 200 high pressure feed pumps or safety pumps class II running on about 50 nuclear sites and cautioned by the N stamp of the American Society of Mechanical Engineers.

120 2)

Its experience in the petroleum industry and water reinjection environmental conditions.

-

Labyrinth seal instead of mechanical seal

-

Choice of environmental equipment and instrumentation

-

Extra safety equipment (especially for lubrication)

We have 35 years of experience in petrochemical processes and 10 years in hi& pressure water reinjection. 3)

Its experience in'turbine design and regulation to design high

efficiency turbine hydraulics, and about 17 years of industrial applications. 4)

Its experience in sea water pumping for the choice and especially the

utilization /of the right materials and the design (40 years in the Middle East and Latin America including off-shore for reinjection, fire pumps, etc.)

IV. THE

1)

TPMDX

Description:

The TPMDX unit is composed of : -

the turbopump TPMDX,

-

the heat exchanger,

-

the gear increaser,

-

the complete lubrication system,

-

the high speed coupling,

-

the low speed coupling,

-

the set of instrumentation,

-

the common baseplate with or without motor,

-

the coupling guards.

The TPMDX turbopump is composed of.: -

one multistage pump (multi-bladenozzle hydraulics),

-

one multistage turbine (multi-bladenozzle hydraulics),

-

one external forced oil lubricated hydrodynamic thrust bearing,

-

one internal hydrostatic bearing located between the pump side and the turbine side, lubricated by handle water,

- only one low pressure labyrinth seal.

121

FEATURES . HYonoBTmc MARIND -THRUST BEAR116

-BARREL DESIGN - LAEYRINTH SEAL

-SURFACE TREATMENT

TPMDX

2)

- RELIABILITY

Flexibility of the design:

As often, the process duties change with time, or are just different than the one expected, it is important to have an adaptable system (membrane characteristics modifications, salinity or temperature slightly different from the design one...)

122 3)

Flexibility

For example: In MALTA both sea water and highly brackish water plants are equipped with the same TPMDX. (Same pump pressure and capacity). Only the turbine nozzles are different to meet the two different recovery ratios: 35% in sea water and 75% in B.W. plant.

MALTA TPMOX %I FOR S. W. AND B. W.

-e-

)

-

Therefore, the B.W. TPMDX can be retrofitted in a few hours to be installed in the sea water plant. 4)

Long range flexibility

As the pumping equipment has to be designed for a 20 years life, and as it is probable that the basic duties of the R/O process will be modified during the coming years, once again, long range flexibility is an important point. Whether or not there is an energy recovery system, the use of a gear increaser is definitely a great advantage on a long range basis.

x, LONO RMOE FLSXIULITY -UEEO MOOlFlCAT~ -

-

.n.

11.1

-e-

-

123

V.

COMPARISON 1)

BETWEEN

Equipment

SEPARATED

AND INTEGRATED

SOLUTIONS

size

The following

sketch

and energy recovery

shows a space comparison

systems

available

between

the different

pumping

~11 units are shown at

on the market.

the same scale.

‘--THE

ENERGY

RECOVERY PUMPING SYSTEMS SIZE DMPARISON

TRAIN OF

L = 7.6m

2)

Technical

L=S

m

comparison

The main causes of failure -

1 - mechanical

-

2 - bearings,

-

3 - wear rings

are:

seals,

(number of stages).

That is why all these elements comparison

in a turbo machine

of the equipment

have to be carefully

to be selected.

considered

in the technical

124

ENERGY

RECOVERY

PUMPING

-TECHNICAL

BEM'IIGS

fgpis SIWTSEAL

COHPARISONSEPARATED

1,NTEGRATED

FE4Tllm

SYSTEN

TPflDX

PELmNmEEL

mxustw

IlWRNAL

1

4 EXTERNAL

I

1 ~HYJRJSTA.

j

+ CLUTCH +6EARIFANY

I

/

$#ljljApDS 1LARYRINTH

I

RALLORSLEEVE

I

4 IEcpALs

2ILc. SEALS

6ullDPACK.

!?%#htis 1

pRSTA6ES

MI,& 3

I

w19: : ] ‘; ,:,,,

TURBINE

4

TO

6

WHEEL

The size and quantity of peripheral equipment (such as.electrical equipment, valves, control...) are two main factors in the cost of a plant. Therefore, such points also have to be included in the cost comparison before making a decision on the equipment to be chosen.

ENERGY

RECOVERY -TECHNICAL

FEAlluE

PUNPING

SEPARATED

INTEGRATED

PRTCNMEEL

REVERSEPlm

TPMDX KW

SYSTEM

CORPARISON-

MGD

KW

M6D

INSTALLED POWER

MAX. 1 SIZINO IS/ID CDNTROL VALVE

STARTIM

1:35 6.5

(268)

BY PASS 20 X TUR.CAP

DIRECT OPEN VALVE

':Z5

a

‘:Yi

10 (450)

10 (450)

&‘p”

TuR,

CAP

CLOSED OPEWINS

~&,p~&LATIDN

VALVE SEOUEMCE

+

125

3)

Efficiency

It is clear that a Pelton running -

pump, whether

1 - The range of high efficiency

the one of a Pelton -

turbine has a greater

2 - The maximum

reverse

efficiency

or not it is of the integral of a reverse

than a reverse

type, for two reasons:

running

pump is smaller

than

turbine. efficiency

of a Pelton

turbine

is higher

than the one of a

running pump.

Nevertheless: -

the difference

in efficiency

decreases

-

the difference

in efficiency

only affects

energy.

For example,

input power, using than the reverse

with increased

capacity.

the turbine recovered

part of the

if a turbine gives a power saving of about 40% of the

a Pelton wheel turbine with an efficiency

running

pump will give an overall

of 3 points higher

saving of about 1% of the

input power. Such a gain is neglegible or choosing

the best control

compared

to the one made by avoiding

maintenance,

system.

.

REVERSE RUNNING PUMP TURBINEB

TURBINE

Efficiency

range from

EFFICIENCY

Efficiency

range from

84 to 86% at design

75 to 85% at design

point.

point.

126 4)

Range of regulation

of turbines

REVERSE RUNNING PUMP TURBINE

PELTON WHEEL TURBINE

razi

RISK OF CAVITATION RANGE

Good adaptability

VI.

OF REGULATION

to capacity

OF TURBINES

Good adaptability

variations

but not to pressure

and pressure

variation,

which affects

technical

efficiency

and

length of life.

RANGE OF APPLICATION It is obvious

decision

It appears

versus

variation

sensibility,

with low but affecting

in both cases.

SYSTEMS

that the size of the needed

equipment

is a major point in the

to choose for the high pressure

pumping

items.

today that 3 ranges of capacities

systems;

solutions

efficiency

OF THE DIFFERENT

of the type of equipment

energy recovery

pumping

both

to both capacity

the following

diagram

define

3 types of high pressure

shows the relative

the range of capacities

interest

they can be applied

to.

TRAIN FRESH WATER PRODUCTION

RELATIVE INTEREST OF DIFFERENT SYSTEMS FOR ENERGY RECOVERY

of the three