EPA-230/1-73-003
OCTOBER, 1973
           ECONOMIC ANALYSIS
                      OF
   PROPOSED EFFLUENT  GUIDELINES

     Cane Sugar  Refining  Industry
                     QUANTITY
      U.S. ENVIRONMENTAL PROTECTION AGENCY
           Office of Planning and Evaluation

              Washington,, D.C. 20460

                          \
                          UJ
                          C3

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This report has been reviewed by the Office of Planning
and Evaluation,  EPA,  and approved for publication.
Approval does not signify that the contents  necessarily
reflect the views and policies of the Environmental
Protection Agency, nor does mention of trade names or
commercial products constitute endorsement or recom-
mendation  for use.

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EPA - 230/1-73-003
                      ECONOMIC IMPACT OF

   COSTS OF PROPOSED EFFLUENT LIMITATION GUIDELINES

        FOR THE CANE SUGAR REFINING SEGMENT OF THE

                   SUGAR PROCESSING INDUSTRY
                          Milton L. David
                        Robert!. Buzenberg
                           October,  1973
                           Prepared for
                  Office of Planning and Evaluation
                  Environmental Protection Agency
                      Washington, D. C.  20460
                                           U.S.  Fnvirc-n'-•-.'-'.?  P.-. •'..-•-': A en Agcpc
                                           Begion o, ;,: -•.   .  < -    •• '*
                                           2150  S. Iij:'...(-.: •  ' :  •-J   .-;•.. :.GVO
                                           Chicago, --.L    Cuj.,4

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             This document is available  in limited
quantities through the U.S. Environmental Protection Agency,
      Information Center, Room W-327 Waterside Mall,
                  Washington, B.C.  20460
        The document will subsequently be available
     through the National Technical Information Service,
                Springfield, Virginia  22151

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                             PREFACE
The attached document is a contractor's study prepared for the Office
of Planning and Evaluation of the Environmental Protection Agency
("EPA").  The purpose of the study is to analyze the economic impact
which could result from the application of alternative effluent limitation
guidelines and standards of performance to be established under sections
304(b) and 306 of the Federal Water Pollution Control Act, as amended.

The study supplements the technical study ("EPA Development Document")
supporting the issuance of proposed regulations under sections  304(b) and
306.  The Development Document surveys existing and potential waste
treatment control methods and technology within particular industrial
source  categories  and Supports promulgation of certain  effluent  limitation
guidelines and standards of performance based, upon an analysis of the
feasibility of these guidelines and standards in  accordance with the require-
ments  of sections 304(b)  and 306 of the Act.  Presented  in the  Development
Document are  the investment and operating costs associated with various
alternative control and treatment technologies.  The attached document
supplements this analysis by estimating the broader economic effects
which might result frot.i  the required  application of various control
methods and technolog es. This study investigate s the effect of alter-
native  approaches  in trrms of  product price  increases,  effects upon em-
ployment and the continued viability of affected plants,  effects upon
foreign trade and other competitive effects.

The  study has  been prepared with the  supervision and review of the Office
of Planning and Evaluation of EPA. This  report was submitted in fulfill-
ment of Contract No. 68-01-1533,  Task Order No. 5 by Development
Planning and Research Associates, Inc.  Work was completed as of
October,  1973

This report is being released and circulated at approximately the  same
time as publication in the Federal Register of a notice  of proposed rule
making under  sections 304(b) and 306  of the Act for the  subject point
source  category.   The study has not been reviewed by EPA and is not
an official EPA publication.  The study will be  considered along with the
information contained in the Development  Document and any comments
received by EPA on either document before or  during proposed  rule making
proceedings necessary to establish final regulations.  Prior to final promul-
gation of regulations, the accompanying study shall have standing  in any
EPA proceeding or court proceeding only to  the extent  that it represents
the views  of the contractor who studied the subject industry.  It cannot be
cited,  referenced, or represented in  any respect in any such proceeding
as a statement of EPA's views regarding the subject industry.

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                            CONTENTS
 I     INDUSTRY SEGMENTS
              A.   Types of Firms
                         1.   Size of Firms
                        2.   Level of Integration
                        3.   Number of P,lants
                        4.   Products
                        5.   Level of Diversification
              B.   Types of Plants
                         1.   Size
                        2.   Locations
                        3.   Level of Technology and  Efficiency
              C.   Number of Plants and Employment  by
                   Segment
              D.   Relationship of Segments to Total Industry

 II     FINANCIAL PROFILE
              A.   Plants by Segment
                         1.   Annual Profit
                        2.   Annual Cash Flows
                        3.   Market (Salvage) Value of Assets
                        4.   Cost Structure
              B.   Distribution of Financial Data
              C.   Ability to Finance New Investment

III     PRICING
              A.   Price Determination
                         1.   Demand
                        2.   Government Sugar Policy
                        3.   Base Point Pricing
                        4.   Supplies
              B.   Expected Price Impacts

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                             CONTENTS

                                                                  Page


 IV     ECONOMIC IMPACT ANALYSIS METHODOLOGY          IV-1
            A.   Fundamental Methodology                        IV-1
                     1.  Benefits                                 IV-6
                     2.  Investment                              IV-7
                     3.  Cost of Capital - After Tax              IV-7
                     4.  Construction of the Cash Flow           IV-9
            B.   Price Effects                                    IV-10
            C.   Financial  Effects     _                            IV-11
            D.   Production Effects                               IV-12
            E.   Employment Effects                              IV-12
            F.   Community  Effects                               IV-13
            G.   Other Effects                                    IV-13

 V      POLLUTION CONTROL REQUIREMENTS AND  COSTS     V-l
            A.   Alternative  Effluent Control Levels               V-l
            B.   Current Level of Control                         V-3
            C.   Water Pollution Abatement Costs                  V-8
                     1.  Investment                              V-8
                     2.  Operating and Ownership Costs          V-14
                     3.  Estimated Costs                         V-14
VI     IMPACT ANALYSIS                                       VI-1
           A.  Price Effects                                    VI-1
           B.  Financial Effects                                 VI-4
                     1.   Profitability                             VI-4
                    2.   Capital Availability Level               VI-7
           C.  Production Effects                               VI-7
                     1.   Potential Plant Closure                  VI-7
                    2.   Sensitivity Analysis                      VI-13
           D.  Employment Effects                              VI-13
           E.  Community Effects                               VI-15
           F.  Balance  of Payments Effects                      VI-15

VII    LIMITS TO ANALYSIS                                    VII-1
           A.  General Accuracy                                VII-1
           B.  Possible Range of Error                         VII-1
           C.  New Technology                                  VII-2
           D.  Critical Assumptions                             VII-3
           E.  Remaining Questions                             VII-3

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                    I.  INDUSTRY SEGMENTS
For identification, this study deals with one of the three functions in the
production of sugar from cane defined by industry code as follows:

                  SIC 2062   Sugar Cane Refining

The other functions, that of cane growing and harvesting and sugar cane
milling (SIC 2061),  have no direct bearing on the  currently proposed
water pollution, but through their indirect activity,  they will be referred
to in several places.
                        A.   Types  of Firms
The firms that own and control the  cane  sugar industry vary from the very
small individual mill or refinery to the giants of U.S. Industry.  By and
large,  large U.S. companies dominate cane  sugar refining and have a
position in cane milling and growing but  no one company has more than
20 percent of a  given segment.

1.  Size of Firms
Table 1-1 lists the  20 large firms that have the dominant position in the
cane sugar industry. Atnstar, by virtue of its five cane  sugar refineries,
and its ownership of Spreckels, a beet sugar company based in California,
has the dominant position in sugar.   Spreckels1  capacity  in beet sugar is
about 12  percent of the U.S. beet capacity and this subsidiary also  has
acquired a -wet corn milling company and are therefore in all phases
of the sweetner industry.

Beyond the 20 large companies that have 77 percent of the refinery capacity
and 34 percent of the sugar cane milling capacity, there  are 60 companies
of various sizes and types that process the rest of that which is considered
domestic cane  sugar production.  These companies are grouped in  specific
areas as seen in Tables 1-2 and 1-3.  The  companies operating refineries
are shown in Table 1-4.

2.  Level of Integration

From Table I-1 it can be seen that there is integration of companies with-
in larger firms and there is a vertical integration in sugar cane production
including growing,  harvesting and cane milling.  Some integration extends
into refining also.

                               1-1

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                 Table 1-1.  Dominant cane sugar firms and relation to industry

1.
z.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.



Firms
Amstar
C & H
Borden, Inc.
Su Crest Corp.
Archer Daniels Midland
CPC International
United Brands
Savannah Foods.
Imperial Sugar
Zapata-Narness
U. S. Sugar Co.
Gulf & Western Foods
Southdown Lands
Jim Walters Co.
Alexander Baldwin Ltd.
A rnfa c
C. Brewer & Co.
Theo H. Davis
Castle & Cooke Inc.
Pepsico
Sub -Total
Other Companies -U.S.
Other Companies - Puerto



Estimated Other Sweetners Cane
Net Worth Corn
($million)
175 X
NA
725
20
124
510 X
494
32
NA
NA
55
673
132
345
143
210
90
NA
224
440


Rican
Beet Grower
X

X
X
X
X
X
X
X
X
X
X




No.


4
2
1
3
1
4
6
8
3
2

34
35
16
Cane Sugar

Mills Refineries
TPD Pet. No.
5
Z
3
2
1
1
1
2
1
14,400 1
18,500
8,000
10,700
4,000
13, 100
17,250
17,300
7,000
7,000
1
117,250 34 20
159,185 45 4
71,500 21 5
TPD Pet.
iU,050
3,690
2,190
1,670
700
1,800
1,200
2*550
1,500
660









800
27,810 77
5,060 16
1,820 7
Total Domestic Cane Sugar Industry
85
347,935  100  29
34,690 100

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Table 1-2.  Raw sugar mill companies by geographical area and
                         number of mills
Location

Louisiana
Puerto Rico
Hawaii
Florida
Total
Table 1-3. Cane sugar
Location

Louisiana
Puerto Rico
Hawaii
Florida
West Coast
East Coast
Texas
Midwest
Total
Number of
Owners
38
12
6
8
64
refinery companies by ge
number of refineries
Number of
Owners
n
"3
1
3
1
8
1
2
I?!/
Number of
Companies
38
16
22
8
84
Number of
Mills
43
16
26
9
94
ographical area and
Number of
Companies

5

3
1
8
1
2
27
Numoer of
Refineries
0
5

3
1
10
1
2
29
I/
   Total doesn't add due to multiregional operations owners.
                               1-3

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                         Table 1-4.   Ownership of domestic refineries
Percent of
 Industry
 Capacity
              Company
   Location
   3Z.9
Amstar Corporation
   11.6


    6.3
    7.4


    1.3

    4.9

    4.3

    5.8

    2.3
California & Hawaiian Sugar Co.


Borden Inc.
   North American Sugar Industries Inc.
      Colonial Sugars Co.
      Florida Sugar Refinery,  Inc.
      Industrial Sugars, Inc.

Savannah Foods & Industries, Inc.
   Everglades Sugar Refinery Inc.

Glades County Sugar Grower Coop Assn.

Godchaux - Henderson Sugar Co.

Imperial Sugar Co.

National Sugar Refining Co.

PepsiCo Inc.
Brooklyn, N. Y.
Boston, Mass.
Baltimore, Md.
New Orleans,  La.
Philadelphia,  Pa.

Crockett, Calif.
Aiea, Hawaii
Gramercy, La.
Belle Glade,  Fla.
St.  Louis,  Mo.

Savannah,  Ga.
C lewis ton, Fla.

Moore Haven, Fla.

Reserve,  La.

Sugarland, Tex.

Philadelphia, Pa.

Long Island City, N.Y.
                                                                   continued--

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                              •  Table 1-4.      (continued)
Percent of
 Industry
 Capacity
              Company
   Location
    3.5
    2.0
    5.2
    1.9
    4.8
    2.0
    5.2
United Brands
   Revere Suyar Refinery

Jim Waiter Company
   The South Coast Corporation

CPC International
   Refined Syrups and Sugars, Inc.

Zapata - Nornuss
   Southdown, Inc.

SuCrest Corporation
Archer Dauielt. Midland
   Supreme Sxigar Refinery

Refineries  of Puerto Rico (5)
Charlestown, Mass.


Ma thews, La.


Yonkers,  N.Y.


Houma, La.

Brooklyn, N.Y.
Chicago, 111.


Supreme, La.

Puerto Rico

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The  cane sugar industry is characterized by a vertical integration which
is far different from the structure than found in the beet sugar industry.
In the beet sugar industry, until this past year, the sugar companies
were separate from the growers and have bargained through growers'
associations for the price  and supply of beets. With the advent of coop
ownership of beet sugar factories, the picture has  somewhat changed
since the beet grower has  an interest in the processing operation.

In cane sugar, the growing of cane and cane  sugar  milling facilities
demonstrates a high  degree of integration through direct ownership
or cooperative organization. Each of the four geographical areas has
its own characteristic as to how integration has developed ove r the years.

Reference to Tables  1-5 and 1-6 will indicate that Puerto Rico  is essen-
tially an integrated operation inasmuch as  the mills' refineries are either
outright owned by the Puerto Rican Commonwealth or subsidized by this
governmental body.  Although there are many small farms, the  growers
are  closely tied to the mills that they are supplying.

In Hawaii, essentially five companies own the  19 mills expected to be
operating in 1973,  and, with the exception of 500 cane growers that have
varying degrees of tie-in with the mills, the cane land is owned  by the
processing mill companies.  In turn, all of these companies and pro-
cessors  own the refinery operations of C&H in Hawaii and on the mainland
near San Francisco.  All of the marketing of sugar is done through this
organization.

Florida has only one mill  that is vertically integrated from growing to
refining, but this  accounts for seven percent of the  Florida raw  sugar
production.  All of the other mills are land owners  and, therefore,
there is  integration of the  grower and the mill covering the 130 farms
in Florida and 90  percent  of the state's  raw sugar production.

Louisiana has  the only area of extensive independent ownership of both
cane farm and milling operations.  Figures are not available to  give a
definite acreage,  but it is  estimated that half of the production in
Louisiana is that of independent growers and independently owned mills.
Seven of the mills owned by three companies are vertically integrated
into  the three operations of the cane sugar industry.
                               1-6

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             Table 1-5.   Cane sugar processing integration relationship,  grower--
                            mill integration,  1971 production
Louisiana
Florida Hawaii
Production Pet Production Pet Production
Total Cane (000 acres)
Total Cane (000 tons)
No. of Farms
Total Raw Sugar (000 tons)
Total Mills
Grower-Mill Integration
Co-op Mills
Administration Cane (000 tons)
Independent Cane (000 tons)'
Total Cane
Corporation Mills
Administration Cane (000 tons)
Independent Cane (000 tons)
Total Cane (000 tons)
Government Mills
Administration Cane (000 tons)
Independent Cane (000 tons)
Total Cane (000 tons)
Total Administration Cane (000 tons)
Total Independent Cane (000 tons)
Total Cane (000 tons)
301
7,974
1,513
571
43

8
2,536
417
2,953
3b
1,663
3,358
5,021
0
0
0
0
4, 199
3,775
7,974
— Total cane acreage - only 1/2 harvested each
Sources: Hawaiian Sugar Planter's Association
Gilmore Sugar Manual 1971

34 194 22
25 6,388 20 10,
130
20 635 23 1,
8

3
86 2,127 99
14 11 1
2, 138
5
33 3,630 85 10,
67 620 15
4,250 10,
0
0
0
0
53 5,757 90 10,
47 631 10
6,388 10,
year due to 22-24 month
Sugar Manual, 1973

232^
685
528
229
19

0
0
0
0
19
151
534
685
0
0
0
0
151
534
685
crop


Puerto Rico Total
Pet Production Pet Production Pet
26 153
34 6,437
4,202
45 324
16

0
0
0
0
0
95 0
5 0
0
16
6,437
0
6,437
95 6,437
5 0
6,437
maturity.


18 880
21 31,484
6,373
12 2,759
86

11
4,663
428
5,091
59
15,444
4, 512
19,956
16
6,437
0
6,437
100 26,544
0 4,940
31,484



100
100

100



92
8


77
23


100
0

84
16




USDA -ASCS various data
Puerto Rico Land Administration Data

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                            Table 1-6.   Cane sugar processing integration relationship, mill-refinery
                                                      integration, 1971 production
CD
Louisiana Florida Hawaii Puerto Rico
Total

Production Pet Production PctProduction Pet Production Pet Production Pet
Total Cane (000 acres)
Total Cane (000 tons)
No. of Farms
Total Raw Sugar (000 tons)
Total Mills
Mill-Refinery Integration
Integrated Mill
Raw Sugar (000 tons)
Non Integrated Mill
Raw Sugar (000 tons)
Total Raw Sugar
— Total cane acreage - only 1/2
301 34
7,974 25 6,
1,513
571 20
43

8
124 22
35
447 78
571
harvested each year due
Sources: Hawaiian Sugar Planter's Assn. Sugar Manual,
Gilmore Sugar Manual
1971
194
388
130
635
8

1
46
7
589
635
to 22
1972.

22 232-/26'
20 10,685 34 6
528 4
23 1,229 45
19

19
7 1,229 100
0
93 00
1,229
-24 month crop maturity


153 18
,437 21
,202
324 12
16

16
324 100
0
0
324
•


880
31,484
6,373
2,759
86

44
1,7^3
42
1,036
2,759



100
100

100



62

38




               USDA-ASCS Various data
               Puerto Rico Land Administration Data

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3.   Number of Plants

The three parts of the cane sugar industry are composed of:

        6,373 Cane  farms or plantations
           85 Cane  mills
           29 Refineries

The previous tables,  1-5 and 1-6,  have given some of the statistics of
integration between farms, mills and  refineries.  Inasmuch as the mills
are  in the middle of the  chain,  it would be well to summarize  the degree
of integration from this  standpoint.  Table 1-5 shows that 84 percent of
the sugar cane  goes to a mill.  Table  1-7 shows that 23 percent of the
refined cane sugar  end-product comes from a mill integrated  with the
refinery.
4.   Products

The cane sugar refining industry is essentially a one product industry ~-
refined cane sugar.   Cane sugar does take on many forms and variations
but the product is  still cane  sugar -- chemically sucrose.  Some sugar
is produced in liquid  form without being crystalized,  but the percent is
very small. _i'  Crystalline  sugar is  produced in varying degrees  of
"olor.. fineness and concentrations.   Still other  combinations include
packaging in bulk, in 100 pound bags.  •-, c m the myriad of Consumer
oacKets,   -..epeatiru-;,  rht- mosi . ornrrion product  .= , /'- = !a ilized white
. ane sugar pricea and solJ ;n  iG'J  oovuni Jaa.

 llit; mili.^ croducc liiroc oy-  roci.1'-1 -^  - x& L>C' ~? - c  ryi o .* a. .^ s e s ,  5.riii 3'i
 rue rmedia '.e, prociucL, raw su;j,ar.  j-3d-,-'°se)  • ne "'uio : rom -he cane,
 •omparabie co some extent \"ith beet  puip iron"  beet ^ugar, : s mo.-'i
frequently used as tuel in the milling process.   In boilers '.esigned :o
handle bagasse  it is burned for energy with  iiatural gas or fuel  oil.
Surpluses are  sold for animal feeds  and some bagasse ends up in  the
building material known as celotex.   Revenue figures from all mills
show almost insignificant income from bagasse  sales.

Molasses  is the important by-product; its prime use is as an animal
feed supplement.   A small percentage becomes  edible molasses for a
variety of food flavorings, colorings  and syrups.  About 3. 6 percent
of the returns to a milling operation comes from molasses.
—  Liquid sugar is common, but most often crmes from putting
    - ••v?talline suqa - into 'iquid form  aite>- tne ^ef-rin :  orores?.

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Table 1-7.  Refinery-mill integration by company and
             relationship to total industry
Refineries integrated
C & H
Glades County Coop.
South Coast
Southdown
Supreme
Puerto Rico
Integrated Refinery Total
Non Integrated Total
Total - All Refineries
Capacity
3,690
460
700
660
700
1,820
8,030
26,660
34,690
No. of
Refineries
2
1
1
1
1
5
11
18
29
Pe rcent
of Capacity
10.6
1.3
2.0
1.9
2.0
5.2
23.0
77.0
100.0
                           1-10

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Summarizing,  the product that shall be most discussed in this report
is refined cane sugar from the intermediate product raw sugar.
5.  Level of Diversification

Referring again to Table 1-1, it can be  seen that the large companies
listed are recognized as  diversified firms.  Cane sugar processing
with few exceptions,  is a small part of  the business for the 20 large
companies.  The notable exception is Amstar which has approximately
60 percent of its inventory in some form of cane sugar and, presumably,
its  sales and assets assume a similar proportion.

The other companies by and large are smaller and primarily derive their
sales from cane  sugar production and processing.
                       B.   Types of Plants
Essentially,  there are three types of plants in the cane sugar industry --
farms or plantations, mills and refineries.  The first and second types,
the farm or plantation, and cane mills, will not be directly considered in
this study.  The  remaining plants or refineries are  distinct and readily
identifiable by name,  size, location and output.

1.   Size
Refineries are industrial plants that operate on a year around basis
as contrasted with the mills that have a seasonal operation which
coincides with the cane harvest.  The tonnage figures in Table 1-8
are raw sugar tons which is approximately 97 percent pure sugar.

As can be anticipated, the larger refineries are in the large population
centers and the nine refineries that have a capacity of over 1,500 tons
per day account for 58 percent of the total U.S.  refining capacity.

With the exception of three plants, all of the refineries  are over 50
years  old and have been well maintained and kept up-to-date.  For  this
reason there is no significant difference in refineries based on age ex-
cept as will be noted under the following section.
                                 I-11

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Table 1-8.   United States cane sugar refinery companies,  location and capacity
No.
Company Name
Refinery Location
Liquid refineries
1
2
3
4
5

Rural: Small
1
2
3
L 4
5
6
7
8

Large
1
2
3
4
SuCrest
Pepsico
Industrial
Florida Sugar
Ponce Candy
.
crystalline refineries - 700 tons/day or less
Glades Co. Cooperative
C & H
Puerto Rico Land Administration
Puerto Rico Land Administration
Everglades
Southdown
Puerto Rico Land Administration
Puerto Rico Land Administration

crystalline refineries - over 700 tons /day
J. Aron
Colonial
South Coast
Godchaux
Chicago, Illinois
Long Island City, N. Y.
St. Louis, Missouri
Belle Glade, Florida
Ponce, Puerto Rico


Moore Haven, Florida
Aiea, Hawaii
Guanica, Puerto Rico
Humacao, Puerto Rico
Clewiston, Florida
Houma , Louisiana
Mercedita, Puerto Rico
Igualdad, Puerto Rico


Supreme- , Louisiana
Gramercy, Louisiana
Mathews, louisiana
Reserve, louioidna
~ ., Total Daily
Capacity '
Capacity
(TPD) (Pet.)
850
800
300
390
100
2 , 440 7

460
190
220
400
350
660
600
700
3,580 10

700
1, 500
700
1, 700
                                                                      4,600
                                                                               (continued)

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Table 1-8.  (Continued)
No. Company Name


Refinery Location Capacity

(TPD)
Total Daily
Ca pa c it y
(Pet.)
Urban: Crystalline refineries
1




2
3
4
5
6
7
8

U. S.
Amstar
M
1C
1 1
II
Imperial
CPC
National
Savannah
Revere
SuCrest
C & H

Total companies (24)
Baltimore, Maryland
Brooklyn, New York
Chalmette, Louisiana
Philadelphia, Pennsylvania
Boston, Massachusetts
Sugar land, Texas •
Yonkers, New York
Philadelphia, Pennsylvania
Port Wentworth, Georgia
Charlestown, Massachusetts
Brooklyn, New York
Crockett, California

Total Daily Capacity
2,600
2, 100
3,250
2, 100
1,000
1,500
1,800
2,000
2,200
1,200
820
3,500
24,070
34,690












70
100

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2.  Locations

Referring to Table 1-8 and Figure 1-1,  the locations of  refineries point
to two of their essential requirements: deep water ports  for shipping of
raw sugar,  domestic and imported,  and close proximity to population
centers and markets.

Raw sugar is not considered a food product and therefore can be shipped
by bulk in cargo ships with a variety of cargo capabilities.  Refined
sugar, on the other hand, is a food and its transport is  at a much higher
rate because  of the sanitary requirements as well as  its higher value.

Sugar refineries have had dockside locations for many years as mentioned
in the previous section on age.  These areas are  highly Industralized now
and for that reason additional land which  may be needed for water pollution
control may be difficult and expensive to  obtain adjacent to the refinery.

This  may not be true of new plants and rural plants (Table 1-8).  The
Chicago and St. Louis  refineries are not deep water port locations
although Chicago is an international port. Raw sugar to St.  Louis  is
shipped by barge up the Mississippi.  Both ports  do qualify for lower
cost transport by water and serve large market areas.

3.  Level of Technology and Efficiency

The cane producing and harvesting part of the industry  is essentially
agricultural and uses  large amounts  of relatively unskilled labor.
Mechanization of the harvesting and loading operations  are increasing
but the equipment is not sophisticated.

Refining is more capital intensive than milling.   This is seen by the
fact that less than  12,000 men refine all  domestic and import raw  sugar as
compared to  15,000 employees for milling which produces only one-third
the amount of raw  sugar the refineries process.  The plants are industrial
in nature and located in industrial areas  as  contrasted  to the agriculturally-
oriented mills.

From Table 1-9 the break-down of plants according to technology is
shown:

                        14  Crystalline refineries
                         5  Liquid sugar  refineries
                         2  Liquid-crystalline refineries
                         8  Refineries operating with mills

Seventy-four percent  of the industry capacity is the normal standardized
crystalline  refinery discussed below.

                                 1-14

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                                                                          ^L    Boston (2)
                                                                        [^^"•SA (Charleston)
                                                                        [tT^^New York (5)
                                                                             (Brooklyn)
                                                                            (Yonkers)
                                                                       .  .(Long  Island City)
                                                                       ''VjRf^&- Baltimore
                                                  New Orleans
                                                    (Chalmette)
                                                 Supreme
                                                 Gramercy
                                                 Ma thews
                                                                 •7  Savannah
                                                                     (Port Wentworth)
 Belle Glade
 Moore  Haven
Clewiston
                                                 Houma
                                                 Reserve
Figure 1-1.  Location of mainland cane sugar refineries.

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              Table 1-9.   Cane sugar refineries by type and capacity


                                                                      Percent of
                                                                    total domestic
Refinery - Type and Company	Location	capacity

Crystalline Refineries

   1.   Amstar                     Baltimore, Md.
   Z.   Amstar                     Boston, Mass.
   3.   Amstar                     Brooklyn, N. Y.
   4.   Amstar                     Chalmette, La.
   5.   Amstar                     Philadelphia, Penn.
   6.   California fe Hawaiian      Crockett, Calif.
   7.   California & Hawaiian      Aiea, Hawaii
   3.   Colonial (Borden)           Gramercy, La.
   9.   Ever glade (Savannah Foods)  Clewiston, Fla.
  10.   Godchaux                   Reserve,  La.
  11.   Imperial                    Sugarland, Texas
  1Z.   National                    Philadelphia, Penn.
  13.   Revere                     Charlestown, Mass.
  14.   Savannah Foods             Port Wentworth, Ga.                  74

Liquid Sugar Refineries

   1.   Florida Sugar (Borden)     Belle Glade,  Fla.
   Z.   Industrial (Borden)         St.  Louis, Mo.
   3.   Pepsico                    Long Island,  N. Y.
   4.   SuCrest                    Chicago,  111.                         1
   5.   Ponce Candy               Puerto Rica
Liquid-Crystalline Refineries

   1.   CPC                       Yonkers, N.  Y.
   Z.   SuCrest                    Brooklyn,  N.  Y.                     8

Refineries Operating with Sugar Factories

   1.   Glades County              Moorehaven, Fla
   2.   Guanica                    Ensenada, P. R.
   3.   Iqualdad                    Mayaquez, P.  R.
   4.   J.  Aron & Company         Supreme, La.
   5.   Mercedita                  Ponce,  P. R.
   6.   Roig                       Yubacoa, P.  R.
   7.  South Coast                Ma thews ,  La.
   8.  Southdown                  Houma, La.                          11
                                 1-16

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 The raw material for cane sugar refining is the raw, crystalline sugar
 produced by the cane sugar factories.  Raw sugar crystals contain a film
 of molasses, the thickness  of which varies with the purity of the sugar and
 in which the non-sucrose components are concentrated.

 The raw sugar processed by the American  refineries may be domestic or
 foreign but from a refining process viewpoint,  there is little difference  in
 raw sugar related to its  source other than the amount of impurities present.

 A cane sugar refinefy receives raw sugar in bulk form by truck, rail, barge,
 and/or ship, and stores  it for periods up to several  months in  large ware-
 houses.

Jlffination and Melting	The first step in the refining process is mingling,
 or placing the raw crystals  into a  syrup solution.  The magma  is fed into
 centrifugals, which separate the syrup and molasses from the  sugar.  Hot
 water is then added to provide a washing action.  The washed sugar is dis-
 charged into a melter which also contains about one-half of the sugar's
 weight in water.

 Clarification (Defecation)-- The screened melt liquor still contains fine
 suspended and colloidal matter which are removed in clarification.  Clari-
 fication may involve coagulation and floatation clarifiers or pressure
 filtration.

 Decolorization--After affination and clarification the sugar liquor still con-
 tains impurities and color that  require  physical adsorption for  removel.
 Most large crystalline refineries use fixed  bed bone  char  cisterns (also
 called filters).

 Sugar liquor passes in parallel through each cistern  in a downward direc-
 tion and undergoes adsorption of the color bodies and ions.  From 90 to
 99 percent of color  is removed, with the higher  percentage removal
 occurring  at the beginning of the cycle.

 Powdered  activated carbon is used for decolorization in small refineries
 and in liquid sugar production.  .Regeneration of powdered carbon is diffi-
 cult and it is normally discarded after one or two cycles.   However,  in
 1972  one company announced the successful and economical regeneration
 of powdered activated carbon.
                 "i.Pti°n adaPted from Develogment Document for Efflux
                 Guideline..
                                  1-17

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   Evaporation--No matter what method of decolonisation is used, the final
   steps of re crystallizing and granulating are essentially the same in all
   refineries.   The first step in re crystallization may be concentration of
   the decolorized sugar liquor and sweet waters in continuous type evapor-
   ators.  Since the liquors in a refinery are kept as highly concentrated as
   possible, refinery pans are relatively small compared with the evapor-
   ators in a raw sugar factory.
Crystallization--After concentration in evaporators,  the  sugar liquor and
sweet waters are  crystallized in single effect,  batch  type evaporators called
vacuum pans.  Several pans are used exclusively for commercial granulated
sugar and the resulting syrups are boiled in other pans.

Finishing--The dryer or granulator is usually a horizontal,  rotating drum
1.5 to 2,4 meters (five to eight feet) in diameter and 7. 6 to 11  meters (25 to
35 feet) long which receives steam heated air along with the sugar crystals.
It may consist of  one drum or more in parallel.  The granulators remove
most of the one percent moisture  still remaining in the sugar after centri-
fugation,  reducing the moisture content to 0.02 percent or  less.  In addition,
the dryers serve  to separate the crystals from one another.  After drying,
the sugar goes to coolers.   Coolers are similar drums, but without the
heating elements.

Any lumps remaining in the sugar are then removed  by fine screening.
Screening also accomplishes crystal size grading.

Other Variations--Four plants representing  seven  percent of total capacity
are  liquid sugar refineries.  The initial refining steps  of affiliation, decolor-
ization,  and even evaporation in a liquid sugar refinery are essentially the
same as in a granulated sugar refinery.   The primary  difference occurs in
the fact liquid sugar refineries do not recrystallize their primary product
and  therefore do  not use vacuum pans for this purpose.  The result  is the
need for considerably less condenser water and process  steam.

Two plants operate both liquid and crystalline refineries and eight are
directly integrated with the cane mills.  These  latter plants refine the raw
sugar directly in much the same manner of the beet  sugar  plants without
the  crystallization and remelt steps.
                                   1-18

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        C.   Number of Plants and Employment by Segment
In the entire U.S. cane  sugar industry,  there was estimated to be a
total of 92, 140 employees in 1970.  This estimate was made up of:

               Subsegment               Number of Employees

                Farm                            64,900
                Mill                             15,000
                Refinery                        12,240
                Total                            92, i40
As  stated, employment in the sugar refineries is low and the industry
is characterized as capital intensive rather than labor intensive.  In
1968 the total employment in refinery operations was estimated  at
13,049.  Since that time,  due to improved efficiency and productivity
(estimated at 1-2 percent per year), 1972 total employment was 12,240.
Table I-10 shows estimated number of employees in each area based  on
the current productivity of 237 employees per 1,000 tons per day refinery
capacity.
           D.   Relationship of Segments to Total Industry
Subsequent financial profiles and impact analyses will depend upon the
use of model plants to represent the various  segmettr.s and  subsegments
of the  cane sugar industry.   The rationale for use of model plants is
largely dictated by the paucity of financial data.  The model plants,
developed to represent the various segments by size, geography and
type, are shown in Table I-11.
                                 1-19

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   Table I-10.  Cane sugar refinery employment by cities in 1970
Location
New Orleans
New York
San Francisco
Philadelphia
Baltimore
Boston
Savannah
Sugar Land
Chicago
Clewiston
Puerto Rico
Sub- total
Other locations
Total
Number employed
2,280
2,541
1,646
1,223
797
982
572
495
215
32
940
11,723
517
12,240
Source:  U.  S.  Cane Sugar Refiners Association, Washington,  D. C. ,
         by  Robert  R.  Nathan,  Assoc. , Inc.
                                1-20

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Table I- 11.  Relationship of segment models to industry for cane sugar refinery segments
Industry
Model
Type

Liquid
Crystalline

Location Size

U rban
Rural Small
Large
Urban Large
Capacity
(TPD)
500
400
1,200
2,000
No. of
plants

5
8
4
12
29
A ve ra ge
capacity
(TPD)
585
409
1, 150
2,005
1,037
Total
(TPD)
2,340
3,680
4,600
24,070
34,690
capacity
(Pet)
7
11
13
69
100

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                    II.   FINANCIAL PROFILE
                       A.   Plants by Segment
Because the  cane s .gar industry is ^ubject to a considerable amount
of government control and allotments, marketing and regulations under
the Sugar Act, there is  a lot of financial data on cane production and
milling which is  av dlable through the Department 01 Agriculture and
th- Sugar Division •.£ the Agricultural Stabilization and  Conservation
Se rvice.

Unfortunately, the fJSDA cost studies exclude the cane sugar refining
segment and therefore subsequent financial data wao constructed from
previous material in an earlier  study entitled "Initial Analysis of Econ-
omic Impact of Wai-^r Pollution  Control Costs Upon U.S.  Cane Sugar
Industry," by ERS .f USDA.» In addition,  other figures were obtained
from the U.S.  Can-- Sugar Refine rics Association and from a  partial
economic study wh  ;h was done  for that association by Robert R.  Nathan
and Associates of "Washington, D. C.  Finally,  in addition to bringing
this  basic materia^ of 1968 up to 1972, a  complete reconstruction was
made and all of the  e data were  then checked with a number of industry
sources represent! 'g various sizes and locations of sugar cane refineries.
1.  Annual Profit

Table II-1 contains  sales and earnings shown in model form for the
two types, liquid  and crystalline,  and the five sizes of cane  sugar re-
fineries.  These data were constructed from a  number of sources and
while none of the  models a re a real refinery, the overall effect does
represent the industry.

Table II-2 are actual figures  of industry totals submitted to the Cost
of Living Council.  For example,  the industry-wide profit for  1972 of
$20 million is  close  to the $25,000, 000 industry profit that a weighted
total of the five model plants would show.   The former figure repre-
sents 91 percent of industry  and the latter figure is 100 percent.
                                II-1

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Table II-l  . Cane sugar refinery models - sales, costs, production and cash flow
Crystalline
Small rural

Capacity(TPD)
Operating days
Production - raw value
Millions hundredweight
Production refined^.'
Millions hundredweight
Sales
Raw sugar
Other costs
Interest
Depreciation
Total costs
Net profit before tax
Net profit after tax
4/
After tax cash proceeds-
Liquid
500
250

2.500
2.336
28, 032
22,659
4, 571
194
140
27, 564
468
243
484
PR.L/
400
250

2. 000
1.869
22, 335
16, 896
5, 430
270
168
22, 764
(429)
(429)
9
Other2/
400
250

2. 000
1.869

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         Table II- 2.   Profit levels of sugar  refineries, 1971-1973
                Number    Percent   Net Profit                Net Profit
                   of         of     Before Taxes    Change    Before Tax
Time Period    Companies  Total       for        From From per 100 Ibs.
                            Industry  Period -      71-72 71-73  Refined
                            Capacity                               Sugar

1971

1972
1st Quarter '71
1st Quarter '72

1st Quarter '73
2nd Quarter '71
2nd Quarter '72

2nd Quarter '73

12

12
12
12

12
11
11

11
%
91

91
91
91

91
89
89

89
$ % %
41, 611, 437
2/
20,239,769- -51.4
10, 194, 362
2,954,662 -71.0
3/
2, 433, 078- -7c. 1
13, 974, 305
8,472,760 -39.0
2/
2,469,634" -82.3
$
2 1 3

. 152
,3.0
. 100

. 080
. 428
. 258

. 077
Source:  U. S.  Cane Sugar  Refineries Assn. ,  Washington,  D.  C. based on
         survey and data filed with Cost of Living Council,  1973.


—  Consolidated data for industry.
—  Includes 3 companies that operated at net loss.
—  Includes 5 companies that operated at net loss.
                               II-3

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Actual industry profits for this time period show a dramatic decline
over the '71 to '73 years and indicates that there are  companies
experiencing losses.

In the model plants the only segment to show a loss was the small
rural refineries which included essentially the four refineries from
Puerto Rico.

Other than the  refineries operating in Puerto Rico, there appears to
be no segment  by  virtue of its size or location that shows loss.  Rather,
as will be shown later, the profitability of refineries  and  of their com-
panies seems to be a function of management and the  philosophy of man-
agement that has been pursued over the years.
                                                                    >
Table II-3  showing the  returns on sales and the returns on investment,
however, indicates an industry with very low returns  and taken a.s a
whole, one  that is not financially healthy and vigorous.

2.  Annual Cash Flows

Estimated annual  cashflows  (after tax earnings plus depreciation) is
displayed in Tables II-1 and II-3.  Positive cash flows were obtained
for all configurations except  the small rural Puerto Rican group.  In
the other four  groups cash flows are similar and there appears to be
no significant difference for each of the four segments that do show a
positive  cash flow.

3.  Market (Salvage) Value of Assets

Data appearing in an earlier  economic study—  showed total asset
values based on hundredweights  of sugar produced. However, the
data which was 1968 data, did seem to have a large margin of error.
Therefore,  in this analysis,  the figures are based on interviews with
knowledgeable  industry people representing a broad section of the re-
fineries  themselves and are based on 1972 figures.
_L' "Initial Analysis of the Economic Impact of Water Pollution Control
   Costs Upon the U.S.  Cane Sugar Industry."  USDA - ERS,  Bruce J.
   Walter and Peter M. Emerson.
                                II-4

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       Table II-3.  Cane sugar refinery models - cash flow,  ROI, ROS
Crystalline
Small rural

Net profit before tax($000)
Net profit after tax($000)
After tax cash proceeds
($000)
Liquid
468
243
484
Total investment- 9,750
($000)
ROI before tax (percent)
ROS before tax (percent)
ROI after tax (percent)
ROS after tax (percent
Cash flow (percent on
investment)
4.8
1.7
2.5
0.9
5. 0
PR
(429)
(429)
9
13, 500
(3.2)
(1.9)
(3.2)
(1.9)
0. 1
Other
431
224
533
13,500
3.2
1.9
1.7
i. G
3. V
Large
rural
1, 008
524
1, 378
28,200
3.6
1.5
1.9
0.8
4.9
Urban
1, 775
923
2,754
41, 250
4.3
1. 5
2.2
0.8
6. 7
—  Estimate,i book value.
                                       11-5

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Estimated Model Plant Investment

The data  shown here in Table II-4 are projected to be the book values
for various model  plants based on 1972 figures.-  Liquid refineries have
somewhat less of an investment than the  crystalline refineries due to a
simplified process and a practice which is quite common in liquid
refineries - that of using higher value raw sugar.  The refining
process is not faced with the removal of  as large a percentage of
impurities as is  necessary in most crystalline refineries that operate
with the world sugar.  Even  though these basic plants are 50 years
old, the machinery and equipment and its value  is current due to
modernization and continual  replacement.  The  land values arc based
on original purchase prices and, therefore, are book values as corn-
pa red to. replacement values  which probably would be  higher.  From
these data, it appears as a rule of thumb that the depreciable  assets
or equipment 'represent approximately one-third of the total investment
in the operation.

Salvage Values

In looking at salvage values as well as investment values, the individual
plants were  considered on their own  merits rather than being part of a
multi-plant company.  Inasmuch as only  one company operates five
refineries, the rest basically operate one  refinery and it was  felt that
the individual unit  should be  considered.   Under multi-plant operations
in the refinery business , however, the working  capital is combined for
the company rather than operated for individual mills and might show a
somewhat different arrangement for  salvage value than has been  indi-
cated here.

In estimating salvage values  in Table II-4, the rationale used was
that net working capital is considered a current asset and therefore
fully recoverable.   Depreciable assets, building and equipment,  are
shown to be  recoverable at approximately  10 percent  of the book  value.
For land,  it is felt that book values  represent market value in a very
conservative appraisal.
                                  II-6

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Table 11- -i,
autj,  i >.i,iic t-ies investmem—  and salvage values
Liquid
Invest- Per-
ui ent cent
21
, ci.,Lial 2.50 100
L)i pi<- i. i.il.li-
-ibddft 3.50 10
Land .50 100
Dol.t 3. 25
lot C.I
in . i t. . , i , .. i , 1 V . / 5
Total
Sdl> ,u,
i /
Kst iin.ii t-d book value.
2/
Mi 1 lu.ii£> ol d^lla rs .
Small Rural Large Rural Large Urban
Invest- Per- Invest- Per- Invest- Per-
Salvat;^ mcui cent Salvage ment cent Salvage ment cent Salvage
2/ 21 21 21 21 21 21
2.50 3.->i) 1UO 3.50 8.00 100 8.00 12.00 100 12.00

.35 5.40 10 .55 10.00 10 1.00 15.00 10 1.50
.50 .50 JOO .50 .80 100 .80 1.50 100 1.50
-].oU 9.40 13.75

Jl.OU 28.20 42.25

3, 3'< 4.55 9.80 15.00




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4.  Cost Structure

In Table II-5, the budgets of cost for the five  segments of model plants
are extremely consolidated to show just basic elements.   The sales are
income figures that are somewhat representative of the published whole-
sale price  of refined sugar quoted in various markets. Below are listed
the 1972 average wholesale prices per hundredweight of refined sugar.

               Northeast                  $13.09
               Chicago and West           12. 00
               Gulf                         12. 14
               Southeast                   12.74
               Pacific                      11.65
               Average U.S.                12.29

While average sale  prices to the distributor reflect these  wholesale
prices, they vary from them due to  discounts and various trade
allowances.  Because the northeast market traditionally carries the
highest wholesale price, the urban refineries show the highest returns
as they are primarily located in this market.

The raw sugar price in the cost budgets bears a consistent relationship
to New York spot prices  which depends on location of the  refinery and
the source of the  raws.  1972 quoted raw sugar prices are shown below:

               Raw  Cane Spot-Price-World     $8.53
               Raw  Cane Spot-Price-Domestic   9.09

The liquid sugar plants traditionally buy a higher purity or higher polarity
domestic sugar than do the crystalline  sugar  refineries.   Since the liquid
refineries normally pay  a premium  for their  raw sugar,  Table II-5 shows
the highest raw sugar price at $9.70 per hundredweight for three plants.

All other refinery costs  vary from a low of $2. 04 for the  liquid plants
to a high of $3.25 for the urban plants.  The urban plants reflect higher
labor and other costs of the urban area in total and the liquid plants
indicate less  costly processing, less investment and, therefore, less
cost to produce liquid  sugar.   The small rural plants of the crystalline
refineries have a higher cost than the other rural plants,  due largely to
the higher costs associated with Puerto Rico.
                               II-8

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                 Table II- 5.  Refinery cost by model size - 1972




Returns
Raw sugar
Other costs
Depreciation
Total costs
Net profit


Liquid

$12.00
9.70
2.04
. 06
11.80
.20

Smal
™i'

$11.95
9. 04
3.05
.09
12. 18
-(•23)

1 rural
Other^*
u , ,
$11.95
9. 04
2.59
.09
11.72
.23
Crystalline

Large rural
• Uf- f A
$12.04
9.09
2.67
.10
11.86
.18


Large urban

$12.72
9.13
3.25
.15
12.53
.19
—  Includes four Puerto Rican refineries.
—  Includes four domestic mainland refineries.
                                      II-9

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Depreciation costs vary from $. 06 per hundred weight for the liquid
refineries to $. 15 for the urban refineries.   This is from 4. 28 per-
cent to 10.0 percent based on the  net asset value.

In estimating income taxes for all model plants,  a straight 4b percent
tax rate was used on earnings.  No carry forward or back provisions
were assumed in  the case of losses.

Summing up the cost structure, it can be  said that raw sugar costs, i.e. ,
raw material,  are the major costs and that equipment and investment are
significant factors.   The industry is characterized as capital intensive
rather than labor intensive.
                 B.   Distribution of Financial Data
As  shown in the preceding discussion of the financial profile  of the
cane sugar industry,  little variance in financial parameters of location
and plant size was found.

Table I-11  shows that the model refineries do closely resemble the
industry quite accurately but in neither case,  the  model plants nor the
real plants, does size or location make a significant difference in
profit or returns.
                                 11-10

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                C.   Ability to Finance New Investment
The ability of a firm to finance new investment for pollution abate-
ment is a function of several critical financial and economic factors.
In general terms, new capital must come from one or more of the
following sources:   (1) funds borrowed from outside sources; (2) equity
capital through the sale of common or preferred stock;  (3) internally
generated funds--retained earnings and the stream of funds attributed
to depreciation of fixed assets.

For each of the three major sources  of new investment, the most
critical set of factors is the financial condition of the individual firm.
For debt financing,  the firm's credit rating, earnings record over a
period of years, stability of earnings, existing debt-equity ratio and
the lenders' confidence in management will be major considerations.
New equity funds through the sale  of  securities will depend upon the
firm's future earnings as anticipated by investors, which  in turn will
reflect past earnings  records.  The  firm's record,  compared to others
in its own industry and to firms in other similar industries, will be a
major determinant of the ease with which new  equity capital can be ac-
quired.  In the comparisons, the investor  will probably look at the trend
of earnings'for the past five or so  years.

Internally generated funds depend  upon the margin of profitability  and
the cash flow from operations. Also, in publicly held corporations,
stockholders must be willing to forego dividends in order  to make earnings
available  for reinvestment.

The condition of the firm's industry  and the general economy are also
major considerations in attracting new capital.  The industry will be
compared to other similar industries (i.e. ,'  other processing industries)
in terms of net profits on sales and on net worth, supply-demand relation-
ships, trends  in production and consumption, the state of  technology,
impact of government regulation,  foreign trade and other  significant
variables. Declining or depressed industries  are not good prospects
for attracting new capital.  At the  same time,  the overall condition
of the domestic and  international economy can influence capital markets.
A firm is more likely to attract new capital during a boom period  than
during a recession.   On the other  hand, the cost of new capital will
usually be higher during an expansionary period.  Furthermore, the
money markets play a determining role in new financing; example, the
1973 year has been viewed as especially difficult for new equity issues.
                             II-ll

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As was seen in Table I-11, there appears to be no significant difference
in the earning ability of a cane sugar refinery based on size or location.
Except for Puerto Rico which is  a special situation and involves com-
panies that are not competing in  the open investment dollar market ,
all earnings  records depend on management.

There are only limited financial  data available for companies •which
operate cane sugar refineries.   Table II-6 presents selected data on
four companies,  three  of which are primarily sugar companies.   The
fourth company,  Southdown, a producer of both raw sugar and refined
sugar, is a widely diversified  company whose operating data are not at
all representative of the cane sugar refining industry.  Although South-
down is included  in the table, it will be ignored in the analysis which
follows.

Profit margins (income before interest and federal income taxes as a
percent of sales) have averaged  in recent years 7.0 percent for Savannah,
6.9 pe rcent for Am star and 3 . 4  pe rcent for Sue rest.  Net income as a
percent of sales  has averaged  2. 5 for Savannah, 2.3 for Amstar and
0.9 for Sucrest.

Net income  as a  percent of net worth has been estimated for Savannah
as 13. 1 (for  two  years,  1970-71), for Amstar as  8. 5 (5-yea r average,
1968-72) and for  Sucrest as 5.7  (5-year average,  1968-72).

Depreciation has averaged three to four percent of gross property values
for these three companies, producing an average cash flow as a percent
of sales  of 4. 1 percent for Amstar and Savannah and  1. 9 percent for
Sucrest.

These three  companies appear sufficiently profitable to be able to
finance new investment.  Sucrest has  a very low profit margin and
earns only about one percent on  sales and five to six percent  on equity.
Its profitability is well below average for manufacturing in general.
At the same  time,  Sucrest has laid out from $1.4 to $3. 1 million
annually for capital expenditures from 1968 through 1972.

The long-term debt situation shows that the three companies  have
from 20 to 30 percent of gross property in fixed debt; Savannah has  a
1972 debt/equity ratio  of 98.3  percent compared to 44.7 percent for
Amstar and Sucrest.  Although Sucrest is highly  leveraged,  the three
companies show  no evidence to indicate that there would be barriers
to borrowing for pollution abatement capital expenditures.
                                11-12

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Table II- 6.  Financial ratios for selected cane sugar refining companies,
                          1968  - 1972
Year
Savannah
Amstar Foods Southdown
Sue rest
Profit Margin (%)
1968
1969
1970
1971
1972
Av.
6.6
5.9
7.3
8.0
6.5
6.9
N.A.
N.A.
7.3
6.7
N.A.
7.0
6.4
19.2
12.6
13.7
15.2
13.4
3.2
3.0
3.7
4. 1
3. 1
3.4
Net Income to Sales (%)
1968
1969
1970
1971
1972
Av.

1968
1969
1970
1971
1972
Av.

1968
1969
1970
1971
1972
Av.
2. 1
1.6
2.5
3. 1
2.4
2.3
Depreciation
3.3
1.7
3.5
3.4
3.4
3. 1
Cash
3.9
3.6
4.3
4.6
4.0
4. 1
N.A.
N.A.
2.9
2. 5
2.0 -'
2.5
to Gross Property (
N.A.
N.A.
3.4
3.5
N.A.
3. 5
Flow to Sales (%)
N.A.
N.A.
4.2
3.9
N.A.
4. ]
22.2
24.6
8.7
9. 1
10.6
15.0
%)
3.4
0.6
3.9
4.3
3.5
3. 1

18.0
19. 1
8.5
9.4
9.9
13.0
1.0
0.8
1.0
1. 1
0.6
0.9

4. 1
4.3
4.3
4.2
4.2
4.2

2. 1
1.9
2.0
2. 1
1.6
1.9
                             11-13

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                      Table II-6.  (continued)
                          Savannah
Year      Amstar            Foods           Southdown          Sucrest

                   Net Income to Net Worth (%)

1968        7.4^          13.6 i/             14.8 i/             4.8^
1969        7.0^          14. 1 U             N.A.               4.6-'
1970        9. 3i/          13.8 I/             N.A.               6.6i/
1971       13.6             1Z.Z                N.A.               7.7
1972        9.7             N.A.                N.A.               4.6
Av.         9.4             13.4                14.8                5.7

              Long-term Debt to Gross Property (%)
1968
1969
1970
1971
1972
Av,
i /
-' 9
28.0
27.2
25.3
22.8
21.0
24.9

months
N.A.
N.A.
31.4
28.9
N.A.
49.0


N.A.
26.7
50.2
54.9
60.3
48.0


41.5
36.9
33.7
31.0
27.8
34.2


.?_' From Report of the Federal Trade Commission on Rates of Returns
   in Selected Manufacturing Industries, Federal Trade Commission,  1961-1970,
   p. 35.
Source:  Standard  and Poor's Stock Market Reports.
                                 11-14

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With respect to the industry's overall ability to fund new investment for
pollution control, the limited data available indicate that some cane  sugar
refineries  may encounter difficulty,  based on recent levels of profitability.
While other factors may influence the decision concerning new investment
in these small refineries,  the low return on investment suggests strongly
that these  resources could be more profitable elsewhere.

It should be noted that these financial analyses have not included
Puerto  Rican refineries.   The picture is complicated by the fact
that the Commonwealth of Puerto Rico owns or  leases  the  company's
properties.
                                 11-15

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                          III.   PRICING
Cane sugar processors are only one component of the sugar industry,
which in turn is a member of the sweetener sector of the U. S.  food
system.  Sugar (sucrose) can be either beet sugar or cane sugar with
cane  sugar accounting for more of the domestic market (see Figure III-l).

Refined beet sugar and cane sugar compete as perfect substitutes in  the
wholesale market.  Through a  quota system the government regulates
the production and importation of sugar  so  as to stabilize and  maintain
prices at-specified levels. Refined sugar is marketed by refiners and
processors under a system of base point pricing.  It will be shown that
the structure of the sugar industry and government policy provides possible
limitations on the sugar processors  ability  to shift the cost of additional
pollution  abatement to the consumers in the long  run.
                           A. Price Determination
1.  Demand

All but a small fraction of domestic sugar consumption is for human food.
U.  S.  per  capita sugar consumption (Table Ill-l)has been fairly stable
since the 1930's,  ranging between 90 and 100 pounds.  Recent increases
above  100  pounds are attributed to the Food and Drug Administration
restrictions on the use of cyclamates.  Sugar and corn sweeteners (corn
syrup  and  dextrose) are known as nutritive sweeteners while cyclamates
and saccharine are called noncaloric sweeteners.  About two-thirds of
all sugar is consumed in industrial uses, especially by food processing
industries.  Only one-fourth is purchased for home use--kitchen and
table.  The remainder is used in restaurant and institutional meal pre-
paration.

Industrial  uses for sugar are mainly in food processing with minor other
industrial  uses (Table III-2 ).  The  beverage industry is the largest user
of sugar and has made little  use of corn sweeteners as a substitute for
sugar.  The beverage industry is also the highest user of noncaloric sweeten-
ers.  Baking,  the next largest user,  has  dropped its use of sugar from
                                 III-l

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PRODUCERS World
Acres
Domestic f '
Acres 35% 1 40% 25%
31 Export Countries 7% 3% 1 5%

PRODUCTS Raw
PROCESSORS


PRODUCTS
_
Sugar
CONSUMERS Market
Sweetenei
Market

Sugar Sugar Cane Sugar Beets Corn
Cane Mills
~T
Raw Sugar
;
! .
Refineries Beet Sugar Wet Corn
1 	 	 — , 	 . 	 , Factories Mills
1 1 !
Refined Sugar Beet Sugar Corn Sweeteners
. 	 i , 	 r |


I 1 	 	
47% i 22% I 31%
• ' "•• 	 — - - — 	 1
1 i ^^^ 	
40% , 19% J 26% 15%

Figure HI-1.  Structure of the domestic sweetener industry.

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Table III-l.   Trends in per capita distribution of nutritive sweeteners ana the
        share that each sweetener represents of the total distribution,
                                1956-71
Calendar
year
1956
1957
1958
1959
1960
1961
1962
1963
1964
1965
1966
1967
1968
1969
1970
1971
1956-67
trend
1968-71
trend
1956-71
trend
Nutritive
sweeteners

110.8
106.4
109.8
109.9
110.9
111 .6
113.1
113.7
113.3
113.6
115.3
114.5
117.7
ilS.l
121.0
122.3
+ .61
+1.67
+ .84
Sugar
Pounds
98.7
94.6
96.9
96.4
97.5
97.7
98.0
97.6
96.2
96.6
98.1
97.2
100.2
100.3
102.5
102.9
+ .04
+ 1.03
+ .34
:Corn sirup: Dextrose

per capita
8.3
8.2
8.7
9.1
9.3
9.7
10.7
11.1
12.2
12.2
12.5
12.6
12.8
13.0
13.1
13.7
+ .46
+ .28
+ .39

refined
3.7
3.6
4.1
4.3
4.1
4.2
4.4
5.0
4.9
4.8
4.7
4.6
4.7
4.8
5.4
5.7
+ .11
+ .36
+ .11
Percent of total
nutritive sweeteners
Sugar
89.1
88.9
88.3
87.7
87.9
87.5
86.6
85.8
84.9
84.9
85.1
84.9
35.1
84.9
84.7
84.1
-.44
-.32
-.34
:Corn sirup
Percent
7.5
7.7
8.0
8.2
8.4
8.7
9.5
9.8
10.8
10.8
10.9
11.0
10.9
11.0
10.8
11.2
+ .37
+ .07
+ .28
Dextrose
3.4
3.4
3.7
3.9
3.7
3.8
3.9
4.4
4.3
4.3
4.0
4.1
-1.0
"' '
4.5
4.7
+ .08
+ .25
+ .06
   Source:  USDA,  ASCS,  Sugar Reports.
                                  Ill-3

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Table  III-2.  Sugar deliveries,  by type of sugar and  by type of product or
                          business of buyer,  calendar year 1971. —
Product or business of buyer
Industrial
Bakery, cereal and allied
Confectionery and related
Ice cream and dairy products.
Canned, bottled, frozen
foods, jams, jellies and
Multiple and all other food


Non-industrial
Hotels, restaurants,
Wholesale grocers, jobbers,
Retail grocers, chain stores,
All other deliveries , in-
cluding deliveries to


Included in totals:
Deliveries in consumer-size
packages (less then 50 Ibs]
Deliveries In bulk (unpack-
aged) 	
Beet
: Cane ;
Imported :
direct
consuciptior. •
Total :

Liquid
Included
Beet
sugar
in totals
: Cane
	 Hunderedweights 2/ 	
9*847,388
6,653,051
4,074,342
11,926,601
9,458,478
4,003,454
282.605
46,245,919
98,375
12.522,604
4.799,114
591.438
18,011.531
64.257,450
9.591.717
25.318.587

17,115,774
14,236,521
7,001,147
35,310.248
11,004,504
5,855,962
1.537.700
92,061.856
1.455.605
30.132.194
21,031,042
1,309.258
53.928.099
145,989.955
41.954.005
34,622.624
161,348
156,920
49,445
50,103
111,587
58,025
40.276
627,704
33,566
542,662
750,163
2.588
1.328.979
1.956,683
652,985
144,527
27,124,510
21,046,492
11,124,934
47,286,952
20,574,569
9,917,441
1,860,581
138,935.479
1,587,546
43,197,460
26.580,319
1.903.284
73.268.609
212,204,088
52,198.707
60,085,738
292,403
167,552
2,150,928
5,831,266
3,564,693
269,138
5<»,002
12.329,982
12,868
345,371
116,833
100 , 84 1
12.905,895
2,377,746
3,269,348
4,783,993
22,768,934
5,325,399
1,585,445
581,339
40,692,204
100,862
311,983
227,642
81.350
721.837.
41,414,041
  y Represents approximately  100.0 percent of deliveries by primary distributors in continental United States.
  21 Reported as produced or Imported and delivered except liquid sugar which is on a sugar solid* content basis.

  Source:  USDA-ASCS,  Sugar Reports. No. 238 (March, 1972), p.  14.
                                                 Ill-4

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80 percent of total nutritive sweeteners in 1956 to less than 74 percent
in 1972.  Sugar's  share of confectionary demand for nutritive sweeteners
has been more stable,  declining from 70  percent  in 1956 to 68 percent in
1C>72.  Although sugar's share of canning demand has fallen from 87 per-
cent in 1956  to 82 percent in 1972,  its share has risen since hitting a low
in 1967.  During the  period  from 1956 to  1972 the  price of corn sweeteners
has fallen relative to sugar  and new production techniques have improved
the quality of corn syrup.

As  shown above, some substitution ,Among sweeteners exists.  Noncaloric
sweeteners are used to meet the demands of those consumers seeking to
limit sugar intake.  Some substitution of  noncaloric sweeteners for sugar
is associated with  relative  price changes.  However,  for  noncaloric
sweeteners quality considerations appear to be more  important.  Corn
sweeteners are sugar's major price competitor.   Technical  improvements
in corn syrup manufacture  have produced a range  of syrups of different
qualities.  Thus,  corn syrup is better able to  meet the different specifica-
tions of users.  A  limiting  factor is the degree of corn  syrup's sweetness
which is less than sugar.   However, research in improving  "corn syrup's
sweetness" is  promising.

Japan's recent development of processes  for the  production of high
levulose and high fructose  corn syrups show  great promise and may
have a significant  impact on the U. S. sweetener market  in the future.
These syrups, produced by partial isome risation  of dextrose (corn
sugar) into levulose, are said to be comparable to sucrose (cane and
beet sugar) in  sweetening power and unlike other corn syrups can be
used as complete substitutes for sucrose.  Thus an improved product
and lower relative prices have made corn syrup a stronger competitor
of suga r.
The substitution of corn syrup is a gradual process and the market reacts
to long-run changes  in prices.  Substitution of corn syrups may require
changes  in manufacturing techniques and alter the quality of the final
product.  Firms making the substitution  must invest  in new  techniques
and develop  promotional programs to "educate" the consun.er to prefer
the new product.  Such difficulties  mean  that the food processor will shift
from one source to another slowly and when the processor can justify the
change for a long period.   In some instances, the  level of use of corn syrup
is restricted by the  Food and Drug Administration.   In other cases, corn
syrup may not be an acceptable substitute thus limiting the extent of
substitutibility.

A price war  beginning in December 1971 among the corn syrup producers
dropped the  equivalent cost ratio of corn syrup to sugar from  70 percent to
36 percent.   Even now as corn syrup prices come up to 7.25 cents  per pound
in New York as of April, 1973, this price is  still  only 55 percent of the
equivalent sugar price in the Northeast (Table III-3).
                                 I1I-5

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Table III-3.  Wholesale prices of sugar,  corn syrup,  and dextrose.
Refined sugar Dextrose
Northeast N.Y.
Year
1956
1957
1958
1959
I960
1961
1962
1963
1964
1965
1966
1967
1968
1969
1970
1971
1972
1973 (April)

8.77
9-15
9- 27
9.33
9.43
9.40
9- 60
11.94
10.68
10. 22
10. 36
10.62
10. 84
11.44
11.97
12.48
13.09
13.31
cents per pound,
7.91
8. 32
8.33
8. 13
8. 13
8. 10
8. 04
9- 10
8. 85
8. 70
8. 87
9.49
9-49
9-96
10. 20
10.71
10.07
10.65
Corn Syrup
N.Y.
dry basis
8.90
9-17
9. 18
9- 10
9.12
9.00
8.73
9. 19
8.36
8. 27
8.34
8.40
7. 85
8.01
8.45
8.77
5.78
7.25
Dextrose
relative
to sugar
90
91
90
87
86
86
84
76
83
85
86
86
86
85
85
86
77
80
Corn syrup
relative
to sugar
101
100
99
98
97
96
91
77
78
81
81
79
72
68

70
44
55
Source: Sugar Reports, USDA-ASCS,  selected issues.
                                   Ill-6

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Production of corn syrup is up and production facilities are fully utilized.
A new entry  into corn syrup production is .Arms tar, a cane  sugar producer
of ''Domino"  sugar and an owner of Spreckels beet sugar division,

Demand and  Price Elasticity

Estimates of price elasticity and cross elasticity of demand for sugar
in industrial uses do not exist.  However,  price consciousness appears
to increase as  the cost of  sugar increases in proportion to total food
costs.  Thus substitution seems to be occurring^  The gradual adjustments
indicate that demand is much more price elastic in the long run as time
for adjustment is increased.

Household use  accounts for about one quarter of total consumption.  Sugar
is a minor item in the household budget.  Households do not appear to
make substitution for sugar when the price  changes.   Estimates of price
elasticity of  demand for household use of sugar confirm this  inelasticity
with estimates ranging from -0. 16 to -0.24.  _'  Likewise, income has
little  influence with income elasticity eslimates  ranging from .03 to
0.15. _   The corn  syrup  price cross elasticity is also small at 0. 05. _'
Thus  households will make little change in  sugar consumption in response
to changes in prices or  incomes.

2.  Government Sugar Policy  —

The U„ S. sugar industry  has been protected and regulated by the
Federal Government since 1789. A quota system of  control was initiated
in 1934 and has been amended and extended periodically since then.  The
current legislation governing the industry is the Sugar Act of 1948 as
amended  in 1971.  This legislation became  effective  January 1, 1972 and
extended  the  Act through December 31,  1974.
—  Thomas H.  Bates and Andrew Schmitz, "A Spatial Equilibrium
   Analysis of the World Sugar Economy, " Giannini Foundation Mono-
   graph No.  24, Univ.  of Calif. , Berkeley,  1969, and P. S. George
   and G. A.  King,  "Consumer Demand for Food Commodities  in the
   U.S. with Projections for 1980," Giannini Foundation, Monograph
   No. 26, Univ. of Calif.,  Berkeley,  1971.

—  Adapted from "Initial Analysis of the Economic Impact of Water
   Pollution Control Costs upon the U.S. Cane Sugar  Industry," Bruce
   J. Walter and Peter  M. Emerson,  ERS, USDA.  (1973)
                                 III- 7

-------
The principal provisions of the U. S. Sugar Act are (a) limitation of the
total supply of sugar available to U. S. consumers, (b) Government sub-
sidy payments to U.  S.  sugar cane and sugar beet growers, (c) an excise
tax on all sugar marketed within the U. S. , and (d) a tariff on sugar imports.

Under the  supply limitation provision  of the Sugar Act, the Secretary of
Agriculture each year (a) determines  the quantity of sugar needed to meet
the requirements of domestic  consumers and to attain the price objective
specified in the Sugar Act, (b) divides, by means of quotas, this total
supply requirement among specified domestic and foreign production
areas, (c) assigns, when necessary for orderly production, "proportion-
ate shares" of each domestic production area  quota to individual farms
within that production area, and (d) imposes,  when necessary  for orderly
marketing, a refined sugar "marketing allotment" upon each refining and
importing  firm.  (See Table III-4  for the 1970, 1971,  and 197Z quotas
assigned to each domestic production  area and foreign country. ) Through
these  strong supply limitation powers granted by the Sugar Act,  'he
Secretary of Agriculture is able to control the price of raw sugar.

The price  objective specified in the Sugar Act is  to maintain the same
ratio between  (a) the price of raw sugar, as registered in the New  York
market, and (b) the average of (i) the  parity index (the index of prices
paid by all farmers for  commodities and services, including interest,
taxes, and farm wages,  1967 =  100) and (ii)  the wholesale price index
(1967  =  100) as the ratio that existed during  the period September  1, 1970,
through August 31, 1971. The Secretary of Agriculture is required to
make  appropriate  adjustments  in his determination of national consump-
tion requirements  whenever the average price of raw  sugar varies from
the objective by 4  percent or more for 7 consecutive days (3 percent or
more  during November, December, January and February).

Sugar marketing is controlled under the provisions of the U. S. Sugar
Act and numerous  changes in the law  since 1934 have  permitted signifi-
cant increases in the output of domestically produced  raw sugar.  Even
larger increases have been granted to domestic  refiners.  Over time,
the increases  granted to each of the domestic sugarcane producing areas
have  been markedly different.   This has affected the degree of moderniza-
tion and the  average size of the mills  producing  raw sugar in each area
although little effect on sugar refineries.

  The Sugar Act provides  for subsidy payments to U. S. sugarcane and
  sugar beet growers.  These payments are made only to growers who meet
  the following conditions:

         a.   That  the grower has  not marketed cane or beets  in excess
              of the proportionate  share for the farm,  as determined by
             the Secretary of Agriculture;

         b.  That  no child labor (except family members) has  been
             employed on the farm;
                                     III-8

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       Table III-4.  U.S. Sugar quotas:  1970, 1971 and 1972 basic and adjusted quotas by domestic production
                                          area and foreign country
1970
Production area
Basic
Quota
Adjusted
Quota — '
(short tons, raw value)
Domestic
Domestic beet
Mainland cane
Hawaii
Puerto Rico
Virgin Islands
Total domestic
JH Foreign
"i"1 Total Foreign
Grand Total

3,597,000
1,308,000
1, 145,486
1, 140,000
15,000
7,205,486

4,394,514
11,600,000

3,
1,
1,


6,

5,
11.

597,000
308,000
145,486
360,000
--
410,486

189,514
600,000
1971
Basic
Quota
Adjusted
Quota U
(short tons, raw value)

3,454,
1,256,
1,110,
1, 140,
15,
6,975,

4,325,
11,300,

000
000
000
000
000
000

000
000

3,
1,
1,


5,

5,
H,

406,333
256,000
110,000
150,000
--
922,333

377,667
300,000
1972
Basic
Quota
(short tons

3,692,
1,643,
1,218,
855,
--
7,408,

4,391,
11,800,

000
000
238
000

238

762
000
Adjusted
Quota I/
, raw va lue )

3,400,
1,643,
1,218,
175,
--
6,436,

5,363,
11,800,

000
000
238
000

238

762
000
—  Adjustments  reflect (a) changes in total U.S.  sugar requirements, (b) withheld quotas,  and (c) deficits and
   deficit prorations.
   Source: USDA-ASCS,  Sugar Reports,  No. 243 (August 1972), pp. 22-24.

-------
       c.   That all employed labor has been paid in full at not less
            than the minimum wage determined by the Secretary;

       d.   That growers who are also processors have paid other
            growers for purchased cane or beets at prices not less
            than those set by the Secretary.

Subsidy payments  provide a powerful financial incentive for growers
to observe the conditions imposed by the Sugar Act.   If a  grower fails
to meet these conditions---!, e. ,  if he attempts to market beets or
cane in excess of his assigned'proportionate shareL-his payments are
reduced  or withheld entirely.  Thus, subsidy payments are the principal
legal device for obtaining compliance by domestic growers, just as
import licenses are the means for obtaining compliance for foreign
suppliers.

Conditional payments are made at the basic rate of 80 cents per  100
pounds of sugar recoverable from the cane or beets grown on farms pro-
ducing less than 350 tons of sugar,  raw value.   The rate declines by
stages to 30 cents per  100 pounds tor all sugar in excess  of 30, 000  tons
produced on a farm.  In addition, growers may  receive payments for
abandoned acreage at the rate of one-third the normal yield for  the  farm;
payments may also be received for  crop deficiencies  caused by
drought, flood,  storm, freezing,  disease,  or  insects which result in
yields  below 80 percent of normal.  Generally,  the payments for aban-
donment and deficiency are much smaller than the conditional payments
made for sugar cane and sugar beets which are  harvested and marketed.
The 1970 and 1946-69 average return to  sugar cane growers,  including
government payments,  are presented in  Table III-5 by production area
and revenue source.

An excise tax is levied on sugar at the rate of 50 cents per 100 pounds,
raw value.  This tax is collected on all sugar  marketed in the United
States   regardless of source.  Receipts  from  the tax in recent, years have
averaged more than $100 million per year, but  payments to sugar cane
and sugar beet growers have averaged about  15  percent less than the tax.
Thus,  the  U. S. sugar  program generates  revenue which is deposited in
the general funds  of the U. S. treasury.  However, it should be noted that
the subsidy payments made under the Sugar Act and the sugar excise tax
are legally separate.   Thus, either one could be amended or repealed
without affecting the other.

The equitable distribution of the benefits which the Sugar Act created was
provided in addition to controlling the supply of  sugar, imposing a tax on
sugar  sales and subsidizing sugar cane and sugar beet growers.  For

                                    III-10

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Table III-5.  Sugarcane growers'  returns by production area and source,  1970 and 1946-69 average.
Production
Area
Louisiana
1946-69 avg.
1970 	
Florida
1946-69 avg.
1970 	
Hawaii
1946-69 avg.
1970 	
Puerto Rico
1946-69 avg.
1970 	

Basis of Payment I/ : Processor Payments : Sugar
Raw sugar :
'per pound/ : (
Cents
6.50
8.19
6.45
8.37
NA
5.93
7.32
: Per ton of sugarcane: :Per ton of
Molasses : produced for sugar .-Total; produced
Act Payments
sugarcane :
for sugar :„_.._.,
per galloi>:s : Molas,e9 : 2/ :: Abandonment
: : : : : deficiency
1,000
Cents Dollars per ton Dollars Dollars
14.73 7.13 .29 43,813 1.24
13.08 9.09 .24 64,629 1.25
14.98 7.86 .28 23,473 .89
14.15 11.67 .27 67,712 1.08
NA NA NA NA NA
11.26 7.92 .35 78,434 1.44
11.63 7.18 .59 45,773 1.08
I/ Seasons' average prices based on selected periods of varying length.
_2/ Seasons' average prices including molasses payment paid by processors to
production.
,37 Less than 0.5 cents.
4/ Includes Commodity Credit Corporation payments for 1945-46.
Source: The Gilmore Louisiana-Florida-Hawaii Sugar Manual. 1971.
per ton
.03
.01
.02
I/
NA
.02
0
growers
and:
1,000
Dollars
7,319
8,692
2,540
6,121
NA
4/15,045
6,341
multiplied
Total Payments
=r ton of sugarcane
produced for
sugar
Dollars per ton
8.68
10.59
9.05
13.02
NA
9.73
8.85
by sugarcane

|Total
1,000
Dollars
51,133
73,321
26,001
73,833
NA
93,898
52,114

          USDA-ASCS, Sugar Reports, various  issues.

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example, most small-scale sugar cane growers have no investment in
the mill to which they sell their cane and usually have little freedom in
selecting a mill.  In most cases, only one or two mills are located near
enough to a given farm to permit the economical transportation of cane.
In order to protect such growers, the USDA annually determines a
minimum price for  sugar cane grown in each of the four domestic pro-
duction areas.  This price  is established by a formula related to the
quality of the sugar cane and the market price of raw sugar for a speci-
fied period.  For most independent growers in most years, this minumum
price is the actual price  received.   The independent grower's ability to
influence the price of sugar cane largely depends,  therelore,  upon the
arguments and evidence which he can present to the Sugar Act administra-
tors who set the  minimum prices.

Imported sugar is sold at the same level of prices paid for domestically pro-
duced  sugar.  Sugar prices in the United States generally have been much
higher than those prevailing in the world market (Table III-6).  During
the past two decades,  world prices have exceeded  the U.  S. price only in
1950-51, 1957-',  1963-64,  and 1972. i'  HighU. S. sugar prices  make  -his
country  a very desirable market for  sugar exporting  nations,  ^specially
those which do not have other preferred markets such ar- the  United
Kingdom or France.  The value of the U. S.  sugar market to  an exporting
nation is also affected by the importance of sugar  exports to that nation's
economy and the share of its sugar exports which  can be sold in the United
States.  In addition  to being the  dominant factor in determining domestic
sugar  prices, the U. S. sugar program is, at times, also an  important
factor influencing world sugar prices.  Each time  that world  sugar prices
have risen sharply, U. S. prices have also risen,  but more moderately.
When world prices have increased,  the Secretary  of Agriculture has
increased the U. S. sugar consumption requirement so as to make more
sugar  available to consumers here.   In 1950,  the increase was from 7.5
million to 8. 7 million tons;  in 1957,  from 8. 8 million to 9. 3 million tons;
in 1963, from 9. 8 million to 10. 4 million tons; and in 1972 from 11.2
million to 11.8 million tons.  In each case,  the increased supply of sugar
for U. S. consumers moderated the price rise here but, by decreasing
supplies available for other importing countries, caused world prices to
rise even further than expected.  Since the United States is by far the
world's  largest importer of sugar--taking 20 to 25 percent of the total
in world trade--unexpected changes in the volume  of  this country's im-
ports have an appreciable effect on all  other  sugar importing  and export-
ing countries.

Although U.  S. sugar prices since the end of World War II have usually
been maintained above the world market level, it does not follow that
U.  S.  prices would have  declined to the world level if quotas had not
—  Exceeded U.S. prices in some months but not for year average.

                              Ill-12

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Table III-6.  Raw sugar prices in New York and the world market,
                               1948-72
Year

1948 	
1949 	
1950 	
1951 	
1952 	
1953
1954 	
1955 	
1956
1957 	
1958
1959
I960 	
1961 	
1962 	
1963 	
1964
1965
1966 	
1967 	
1968 	
1969 	
1970 	
1971
1972

Raw sugar in
Now York

..- 5.54
..: 5.81
5.93
6.06
..: 6.26
6.29
6.09
..: 5.95
..-. 6.09
..: 6.24
..: 6.27
6.24
6.30
6.30
6.45
. . : 8 . 18
.. : 6.90
..: 6.75
..: 6.99
..: 7.28
..: 7.52
..: 7.75
..: 8.07
..: 8.52
..: 9.09

World sugar I/ ]
	 Cents per pound------
5.13
5.03
5.82
6.66
5.08
4.27
4.14
4.19
4.47
6.10
4.36
3.86
4.09
3.85
3.87
9.41
6.79
3.07
2.81
2.95
2.96
4.37
4.88
5.65
8.53

Difference :
New York
over
world

0.41
0.78
0.11
-0.60
1:18
2.02
1.95
1.76
1.62
0.14
1.19
2.38
2.21
2.45
2.58
-1.21
0.11
3.68
4.18
4.33
4.56
3.38
3.19
2.87
0.56

  Tj Adjusted to the New York delivery  base.

  Source:  USDA-ASCS, Sugar Reports.
                                  Ill- 13

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existed and import duties were unchanged.  Without quotas,  U.  S.  prices
would have  declined and those in the world market would have risen until
they balanced at some intermediate level.  No estimates of changes in
U. S. and world prices,  based on various assumptions  regarding changes
in quotas and tax policies,  are available.

The U.  S.  sugar program has both benefited the domestic sugar industry
and increased the average price paid by sugar users.  The disadvantage
to consumers of higher sugar prices  has been partially offset by the bene-
fit of extreme price stability relative to the prices  of other agricultural
products.

The Secretary of Agriculture also must adjust quotas for domestic areas.
For example, should the effluent limitation guideline costs close mills
and production is abandoned, the Secretary of Agriculture  is required by
law to distribute these acreages to other domestic quota areas first and
then to  import quotas.  The Secretary is directed to set quotas  for the
coming year such that the price objective for raw sugar as defined in  the
law is satisfied. If abandoned production was  not reallocated, there would
be a short  run shortage  of sugar forcing wholesale  prices up causing re-
finers to bid up the price of raw sugar,  and thus causing divergence away
from the price objective.

3.  Base Point Pricing

Base point pricing developed because large refineries found  it economical
to locate close to ports of entry or adjacent to major population centers.
This gave them ready access to off-shore sugar from which  the bulk of
refined  cane sugar is manufactured.  Because these refineries  became
the major sellers in their respective  areas, they established base point
pricing. Eight  points of  origin are used in this base point  pricing.  Within
a region the price at any point is the  origin sugar price plus the freight
cost from base  point to the buyer's location.  The principal seller in a
region sets the  price so as to maximize his profit in the region. All
sellers  of sugar compete to sell their excess sugar in the Chicago market.
The Chicago market has  been used because many food processors are
located  there  and because the nation's rail system tends to come together
at Chicago.  Thus the result of base point pricing is a lower price in
Chicago as  can  be seen in Table III-7.  Obviously,  the wholesale market
for sugar is not one of perfect competition.
                                Ill-14

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Table III-7 . Wholesale prices for  refined sugar, March 1973.
100 Ib. bag
Location
Northeast
Midcentral
Western Ohio-Lower Michigan
Southeast
Gulf
Chicago - West
Intermountain North
Pacific Coast

1
1
1

3.
2.
2.
12.
1
1
1
1
2.
1.
2.
1.
cents per
31
85
20
95
40
75
05
85
bulk
Ib.
12.
12.
12.
12.
12.
11.
11.
11.

70
25
05
45
05
55
80
70
 Source:  Sugar Reports,  USDA-ASCS (April,  1973).
                               Ill-15

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4.  Supplies

In the total supply of sugar for the U.S. , imports play a major role.
Forty-five percent of this total supply is imported, 26 percent of the
total comes from domestic sugar cane,  and 29 percent from domestic
sugar beets.


                    B.   Expected Price  Impacts
Since the demand for sugar for household use  is relatively inelastic,  we
doubt that a price increase would alter the  consumption patterns signi-
ficantly.  Although price elasticities for  industrial uses  or cross elas-
ticities with other sweeteners, such as beet sugar, corn  sweeteners and
synthetics,  are not known with certainty, this market representing about
two-thirds of sugar use appears to be price conscious and with the in-
direct government price controls oriented toward  price stability,  it is
doubtful that significant price increase;, can be achieved in the  long run
by the cane sugar industry to offset investment :ri  non-proau<. tr. e pollu-
tion control equipment.

The price situation is further compounded by  the role of sugar  imports,
which  represent about  45 percent of total sugar  consumption.  Also in-
fluencing expected price impacts will be  the response of the beet sugar
industry to pollution controls.  However, it should be noted  that in an
analysis of the impacts on  the beet sugar industry—'  it was  concluded
that imposition of water pollution controls would not  significantly in-
crease prices  due to the large amount of in-place  control currently being
achieved.

The ability of the industry  to pass along cost increases will ultimately
depend on government  sugar policy.  Supply curtailment  in the  cane mill
segment could mean price  increases to refiners and  consumers, if quotas
are not adjusted accordingly and world sugar  prices  remain at  present
levels.  Any significant curtailment of U. S. domestic cane  production
could mean that the exceptionally strong  world sugar prices will continue,
since U.  S. actions tend to impact  the world price, as pointed up above
in the  discussion of government sugar policy. At the present stage of
analysis, we suspect that much of the projected price effect will depend
on the impact on cane mill production.
 ~J Economic Impact of Costs of Proposed Effluent Limitation Guide-
   lines for the Beet Sugar Industry, Draft Report, Development Planning
   and Research Associates , Inc.,  (1973).
                                Ill-16

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       IV.  ECONOMIC IMPACT ANALYSIS METHODOLOGY
The following economic impact analysis utilizes the basic industry infor-
mation developed in Chapters I-III plus the pollution abatement technology
and costs provided by Environmental Protection Agency.  The impacts
examined include:

               Price effects
               Financial effects
               Production effects
               Employment effects
               Community  effects
               Other effects

Due to the crucial nature of potential plant shutdowns (financial and
production effects) to the other impacts, a disproportionate amount of
time will be  devoted  to the  financial and plant closure analysis.

In general,  the approa.ch taken in the impact analysis is the same as that
normally done for any feasibility capital budgeting study of new invest-
ments.   In the simplest of  terms, it is the problem of deciding whether
a commitment of time or money to a project is worthwhile in terms of
the expected benefits  derived.  This decision process is complicated by
the fact that benefits will accrue  over a period  of time and that in prac-
tice the analyst is not sufficiently clairvoyant nor physically able to re-
flect all  of the required information, which by definition must deal with
projections of the future, in the cost and benefit analysis.  In the face
of imperfect and incomplete information and time constraints, the industry
segments were reduced to  money relationships insofar as possible and the
key non-quantifiable  factors were incorporated into the analytical thought
process  to modify the quantified data.  The latter process is particularly
important in view of  the use of model plants in  the financial analysis.  In
practice, actual plants will deviate from the model and these variances
will be considered in interpreting financial results based on  model plants.
                   A.   Fundamental Methodology

      Much of the underlying analysis regarding price, financial, and produc-
      tion effects is common to each kind of impact.  Consequently, this case
      methodology is described here as  a unit with the specific impact inter-
      pretations being discussed under the appropriate headings following this
      section.
                                     IV-1

-------
The core analysis for this inquiry was based upon synthesizing physical
and financial characteristics of the various industry segments through
model or representative plants.   The estimated cash flows for these
model plants are summarized in  Chapter II.  The primary factors involved
in assessing the financial and production impact of pollution  control are
profitability changes, which are a function of the  cost of pollution control
and the ability to pass along these costs in higher prices.  Admittedly,
in reality,  closure decisions are  seldom made on a set of well defined
common economic rules, but also include a wide  range of personal values,
external forces such as the ability to obtain financing or consideration of
production unit as an integrated part of a larger cost center  where total
profit center must be considered.

Such  circumstances  include but are  not limited to  the following factors:

        1.   There is a lack of knowledge on the part of the owner-
            operator concerning the actual financial  condition of  the
            operation due to faulty or inadequate accounting  systems
            or procedure:;.   This  is especially likely to occur amont/
            small, independent operators wao tiu not have eife*. T^/K
            cost accounting systems.

        2.   Plant and equipment are old and fully depreciated and the
            owner has, no intention of replacing or modernizing them.
            He can continue in production as long as he can cover labor
            and materials costs and/or until the equipment deteriorates
            to  an  irrepairable and inoperative condition.

        3.   Opportunitites for changes  in the ownership structure of the
            plants (or firms) exist through the acquisition of the  plants
            by grower cooperatives  where the principal incentive is that
            of maintaining  sugar  caneacreages in situations where
            grower  returns from sugar cane production are substantially
            above returns from alternative cropping opportunities.  In
            this situation, which  presently exists in the cane sugar in-
            dustry,   growers may elect to form producer-processor
            cooperatives and acquire ownership of processing plants
            which they would continue to operate at levels of return
            generally unattractive to private owners.

        4.   Personal values  and  goals associated with business ownership
            that override or  ameliorate rational economic rules  is a
            complex of factors commonly referred to as a value  of psychic
            income.
                                 IV-2

-------
       5.  The plant is a part of a larger integrated entity and it either
           uses raw materials being produced profitably in another of
           the firm's operating units wherein an assured market is
           critical or, alternatively, it supplies raw materials to
           another of the firm's  operations wherein the source of supply
           is critical. When the profitability of the second operation
           offsets the losses in the first plant,  the  unprofitable oper-
           ation may continue indefinitely because the  total enterprise
           is profitable.

       6.  The owner-operator expects that losses are temporary and
           that adverse conditions will dissipate in the future.  His
           ability to absorb short-term losses  depends upon his access
           to funds,  through credit or personal resources  not presently
           utilized in this particular operation.

       7.  There are very" low (approaching zero)  opportunity costs for
           the fixed assets and for the  owner-operator's managerial
           skills  and/or  labor.   As  long as the operator can meet  labor
           and materials costs,  he will continue to operate.  He may
           even operate with gross revenues below variable costs  until
           he  has exhausted his working capital and credit.

       8.  The value of the land on which the plant is located is appreci-
           ating at a rate sufficient to offset short-term losses, funds
           are available  to meet operating needs and opportunity costs
           of the  owner-operator's managerial skills are low.

The above factors, which may be at variance with common economic
decision rules, are generally a ssociated with proprietorships and
closely held enterprises rather than publicly held corporations.

While the above factors are present in and relevant to business decisions,
it is argued that common economic  rules are sufficiently universal. To
provide an useful  and  reliable  insight into potential business  responses
to new investment decisions,  as represented by required investment in
pollution control facilities,  economic analysis will be used as the
core analytical procedure.  Given the pricing conditions, the impact on
profitability (and possible closure) can be determined by simply computing
the  ROI (or any other profitability measure)  under  conditions of the new
price and incremental investment in pollution control.  The primary con-
sequence of profitability changes is the  impact on the plant in terms of  a
plant shutdown rather than making the required investment to meet
pollution control requirements.
                                  IV-3

-------
In the most fundamental case, a plant will be closed when variable ex-
penses  (Vc; are greater than revenues (R),since by closing the plant
losses can be avoided.  However, in practice, plants continue to operate
where apparently Vc > R.   Reasons for this inciude:

        •  lack of cost accounting detail to determine when Vc > R.

          opportunity cost of labor or some other resource is less
          than market values.   This wouid be particularly prevalent
          in proprietorships where  the  owner considers his labor as
          fixed.

          other persona) and external financial factors.

          expectations that revenues will shortly increase to cover
          variable expenses.

A more probable  situation  is the  -~ase "/hore Vc ^ R. but revenues  ?.re
less than /arinblo . ^-r. ? plus .-j-h eve rht-:-.c  ...-cp.-.-nse s  .TCv-) n-hich '.re
fixed in the siiori run.  11 this .situation ^ print would  continue to <:per-
ate as tonkas -'ontributions are be in 15 inatU;   , ward covering a port um  or
these fixed  cash  rvf mead •-.•xoetise s.   Tiio :  rm .varmct ope i .lie iiiaef'mi-v iv
under tnis condition.  ->ut ir.e icngLr. ot r.his oor;cu is uncertain.  Lasic it.
'his strategy of continuing  operations is the  zVrrrvs  expectaticn r.hnt re-
venues  will increase ^o cover cash, outlays.  Factors involved in this  tvpe
of closure decision include:

          extent of capital resources.  If the owner has other business
          interests or debt sources that will supply capital input,  the
          plant \vill continue.

          lack of cost accounting detail or procedures to know that TCc>R,
          particularly in multiplant business situations.

          labor or other resources  may be  considered fixed and the
          opportunity cost for these  items is less than market value.

Identification of plants where TCc >  R  but Vc < R leads to an estimate
of plants  that should be closed over  some period of time if revenues  do
not increase.  However,  the timing  of such  closures is difficult to predict.

The next  level of  analysis, where TCc ^ R,  involves estimating the
earnings  before and after investment  in pollution abatement.  So long
as TCc   R  it seems likely that investment in pollution control will be
made and plant operations  continued  30  Ions as the  capitalized value
                                IV-4

-------
of earnings (CV), at the firms (industry)  cost of capital, is greater
than the  scrap or salvage value  (S) of the sunk plant investment.  If
S > CV,  the firm could  realize  S in cash and reinvest and be financially
better off.  This presumes  reinvesting at least at the firms (industry)
cost of capital.

Computation of CV involves discounting the future earnings flow to
present worth through the general discounting function:
                                         A  (Hi)-n
                                n=l

                      where

                      V     =   present value
                      An    =   a future value in n**1 year
                      i      =   discount rate as  target ROI rate
                      n     =   number of conversion products, i.e.,
                                1 year, 2 years, etc.
                      t     =   terminal number (or year)
It should be noted that a more common measure of rate of return is
the book rate,  which measures the after-tax profits  as a ratio of in-
vested capital, net worth, or sales. These ratios should not be
viewed as a different  estimate of profitability as opposed  to DCF
(discounted cash flow) measures but rather as an entirely different
profitability concept.  The reader is cautioned not to directly compare
the DCF rates  with DCOK  rates.  Although both measures will  be  reported
in the analyses, the book  rate is reported  for informational purposes  only.

The two primary types of DCF measures of profitability are used.  One
is  called the  internal  rate of  return or yield and is the computed discount
rate (yield) which produces a zero present value of the cash flow.  The
yield  is the highest rate of interest the investor could pay if all funds
were  borrowed and the lean was returned from  cash  proceeds of the
investment.  The  second DCF measure is  the net present value concept.
Rather than solve for the  yield,  a discount rare equivalent to the firms
cost of capital  is used.  Independent investments  with net present values
of above zero are accepted; those below zero are rejected.  The concept
of comparing capitalized earnings with the sunk investment value is
a variation of the  net  ore sent value method.
                                IV-5

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The data input requirements for book and DCF measures are derived,
to a large extent, from the same basic information although the final
inputs are handled differently for each.

1.  Benefits
For purposes of this analysis,  benefits for the book analysis have been
called after-tax income and for the DCF analysis after-tax cash proceeds,
The computation of each is shown below.
       After tax income    =      (l-T)x(R-E-I-D)


       After tax cash proceeds   =   (1 -  T)x(R - E - D)  + D

       where

               T    =    tax rate

               R    =    revenues

               E    =    expenses other than depreciation and interest

               I =   =    interest expense

               D    =    depreciation charges

Interest in the cash proceeds computation is omitted since it is  reflected
in the discount rate, which  is the after-tax cost of capital, arid will be
described below.   Depreciation is  included in the  DCF measure only ia
terms of its tax effect and is then added back so that a cash flow over
time is obtained.

     A tax rate of 48 percent  was used throughout the analysis.  Accelerated
     depreciation methods, investment credits, and carry forward and carry
     back provisions were not used  due  to their complexity and special limi-
     tations.  It is  recognized that in some instances the effective tax rate
     may be lower  for single  plant but,  with the dominance of multiplant
     firms, the industry's tax rate will  be  close to  the 48 percent rate.

     Revenue,  expenses, interest and depreciation  charges used were those
     discussed in Chapter II.   Chapter V discusses the cost of pollution con-
     trol facilities. These items were assumed to  be  constant over the
     period of  analysis.
                                    IV-6

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2.  Investment

Investment is normally thought of as oatlays for fixed assets and working
capital.  However, in evaluating  closure of an on-going plant where the
basic investment is sunk,  the value of that investment must be analyzed
in terms of its liquidation or salvage value,  that is its  opportunity cost
or shadow price. _'  For purposes of this  analysis,  sunk investment was
taken as the  sum of equipment salvage value plus  land at book value plus
the value of the net working capital (current assets less current liabilities)
tied up by the plant (see Chapter  II for values). This same amount was
taken as a negative investment in the terminal year.  Replacement  in-
vestment for plant maintenance was taken as equal to annual depreciation,
which  corresponds to operating policies of some managements and  serves
as a good decision rule for replacement in an on-going business.

Investment in pollution control facilities was taken as the estimates
provided by EPA and shown in Chapter V.  Only incremental values
were used to reflect  in-place facilities.  The value of the land involved
was taken as a negative  investment in the terminal year.

The above discussion refers primarily to the DCF analysis.  Investment
used in estimating book rates was taken as  invested capital--book value
of assets plus net working capital.  In the case of new investment,  its
book rate was estimated as 50 percent  of the original value.

3.  Cost of Capital - After Tax

Return on invested capital is a fundamental notion in U. S.  business.
It provides both a measure of actual performance of  a firm as well as
expected performance.  In this  latter case, it  is also called the  cost
of capital. The cost of capital is defined as  the weighted average of
the cost  of each type of capital (equities and interest bearing liabilities)
employed by  the firm.  There is  no methodology that yields the precise
cost of capital,  but it can be' approximated within reasonable bounds.

The cost of equities was estimated by two me thods -- the dividend yield
method and the earnings stock price (E/P ratio) method.  Both are
simplifications of the more complex DCF methodology.   The dividend
method is:
—  This should not be confused with a simple buy-sell situation which
   merely involves a transfer of ownership from one firm to another.
   In this instance, the opportunity cost (shadow price) of the invest-
   ment may take on a different value.
                               IV-7

-------
               k  =  --  +g
                     p    8
      where
               k  =  cost of capital
               D  =  dividend yield
               P  =  stock price
               g  =  growth

      and the E/P method is simply

               k  =  E/P
      where   k  =  cost of capital
               E  ~  earnings
               P  =  stock price

and is a further simplication of the first.   The Latter assumes future
earnings as a  level, perpetual stream.

The after tax cost oi debt capital \* a s  pstimatc-d by us me; reported micros;
costs as a percent ot total debt ana n-, iitiply.n>; '.;y . ~ Z - - assurr.mr o 48 pi r-
cent tax rate.   These  values were '.vei^n'.^u o\ ihc- respective cquilv  u> tola]
asset and total liabilities L' to total asset  ratios.

The average cost of capital for the su
-------
 As shown in the above computations, the estimated after-tax cost is 6.8
 to 8. 5 percent.  The  subsequent analysis was based on 6. 5 and 7. 5 percent,
 since it was felt that  this was representative of the industry.  However,
 the above 6.8 to 8.5 percent were estimated from only four firms.  The
 lower estimate presumes a four percent growth factor which is roughly
 equal to inflation expectations.

4. Construction of the Cash Flow

A twenty-two period cash flow was used in this analysis and was
constructed as follows:

       1.   Sunk investment (salvage market value of fixed assets  plus
            net working capital) taken in year t  .

       2.   After tax cash proceeds taken for years tj to t2Q-

       3.   Annual replacement investment  equal to annual current
            depreciation taken for years tj to
       4.   Terminal value equal to sunk investment taken in year t2j-

       5.   Incremental pollution control investment taken in year tQ
            for 1977 standards and year  t^ for 1983 standards.

       6.   Incremental pollution expenses taken for years tj to t^g
            for 1977 standards and years t., to t2Q for 1983 standards,
            if additive to the  1977 standards.

       7.   No replacement investment taken  on incremental pollution
            investment on the assumption of a 20 year life.

       8.   No terminal value of pollution facilities was taken in year I,,, .
            Often land would  be taken,  but because it represents such
            a  small quantity,  the value was ignored.

-------
                         B.  Price Effects
At the outset, it must be recognized that price effects and production
effects are intertwined with one effect having an impact upon the other.
In fact, the very basis of price analysis is the premise that prices and
supplies (production) are functionally related variables which are simul-
taneously resolved.

Solution of this requires knowledge  of demand growth, price elasticities,
supply elasticities,  the degree to which regional markets exist, the degree
of dominance experienced by large firms in the industry, market concen-
tration exhibited by both the industry's suppliers of  inputs and purchasers
of outputs, organization and coordination within the  industry,  relation-
ship of domestic output with the world market,  existence and nature of
complementary goods,  cyclical trends  in the industry,  curreat utilization
of capacity and, exogenous influences upon price determination (e.g. ,
governmental regulation).

In view of the complexity and diversity of factors involved in determin-
ation of the market price, a purely quantitative approach to  the problem
of price effects is  not feasible.  Hence, the simultaneous considerations
suggested above will be made.   The judgment factor will be  heavily em-
ployed in  determining the  supply response to a price change and altern-
ative price changes to be employed.

As a guide to the analysis of price effects, the estimated price  required
to leave the model plant  segment as well off as it is today will be computed.
The  required price increase at the  firm level will be  evaluated in light of the
relationship  of the model plant to the industry and the understanding of
the competitive position of the  industry.   The required price increase can
be readily computed using the DCF analysis described  above, but dealing
only with the incremental  pollution investment and cash proceeds.

Application of the above DCF procedure to these costs  will yield  the present
value of pollution control costs  (i.e. , investment plus operating cost less
tax savings).  If this is  known, the price increase required to pay for
pollution  control can readily be calculated by the formula
                                    IV- 10

-------
                             (PVP) (100)
                      X  -   (1-T)  (PVR)

       where:

           X   =   required percentage increase in price

          PVP =   present  value of pollution control  costs

          PVR  =   present  value of gross revenue starting in the year
                    pollution control is imposed
             T  =   tax rate
Note that this formula implies that incremental profits resulting from
the price increase, will be taxed at a rate of 48 percent.


                        C.    Financial Effects
In Chapter II, the financial characteristics of model plants were presented.
These data will serve as the base point for the analysis of financial effects
of pollution control.  The primary focus of analysis will be upon profit-
ability in the industry and the ability of the firms to secure external
capital.  Hence, it is ob%rious that this portion of the analysis cannot
be divorced from production effects since profit levels and the ability
to finance pollution abatement facilities will have a direct influence on
supply responses --  utilization of capacity and plant closures.

The measures of profitability utilized will include after-tax book rate
of return on invested capital and cash flow (after-tax profit plus
depreciation).  After-tax profit as a percent of sales will
also be reported to assist in comparing financial data  with standard
industrial measures.

In addition to  these factors, two  additional measures of economic profita-
bility will also be examined:  (1) capitalized value of earnings and  (2)
present values estimated by the procedures described in  Section A above.
Both of these  measures will be calculated on pre- and post-pollution control
bases.

Given these financial measurements,  the ability of the industry to
finance the  required  pollution control expenditures will be reexammed
in light of the financial results and the information shown  in Chapter II.
This ability will vary from one industry subsector to another due to
different financial structures, profitability, and abatement requirements.
Hence,  capital availability and cost will probably have to be examined on
a model plant by model plant basis.

                                   IV- 1 1

-------
                    D.  Production Effects
Potential production effects include reductions of capacity utilization
rates,  plant closures and stagnation of industry growth.  It is antici-
pated that reductions in capacity utilization will be estimated via quali-
tative techniques given the analysts' knowledge of the industry.   The
same is true for assessing the extent to which plant closures may be
offset by increases in capacity utilization on the part of plants remaining
in operation.  Data limitations and time constraints are expecced to re-
quire that the impact of pollution control standards upon future  growth
of the industry also be estimated via qualitative methods.

The remaining effect,  plant closures, is very difficult to measure
realistically as discussed above in Section A. As  a starting point
in the plant closure analysis, a shutdown model will be employed
to indicate which model plants should be closed, the marginal oper-
ations  and the sound operations.  These conclusions will be based upon
the decision rule that a plant will be closed when the net present value
of the  cash flow  is less than zero.

It is recognized  that the use of models to represent an industry is
imperfect and that not all of the  relevant values  or factors can be
included in the models. Hence,  in this industry, the appropriate
model plant results will be equated with e^ch cane sugar plant and
the variances to the model plant parameters will be subjectively eval-
uated to arrive at an estimate of the probability of closure.
In Chapter VI a list of the 6 model parameters are shown against  which
eacn plant in the industry was compared.
The above analysis will be done under a'without pollution "control condi-
tion and a"with pollution"control condition.  The former (and including
historical trends) will establish a baseline against which total closures
after pollution control will be compared,  to arrive at an estimate of
closures due to pollution control.
                      E.  Employment Effects
Given the production effects of estimated production curtailments, plant
closings and changes in industry growth, a major  consideration arises
in the implications of these factors upon employment in the industry.
The employment effects stemming from each of these production  impacts
will be  estimated.  To the  extent possible, the major employee classifi-
cations involved will be examined with respect to the potential for re-employment.
                                  IV-12

-------
                      F.   Community Effects
The direct impacts of job losses upon a community are immediately ap-
parent.  However, in many cases, plant closures and cutbacks have a
far greater impact than just the employment lost.  Multiplier effects
may result in even more unemployment.  Badly needed taxes for vital
community services may dwindle.  Community pride and spirit may be
dampened.  However, in some  cases, the negative community aspects
of production effects  may be very short-term in nature with the  total
impact barely visible  from the  viewpoint of the overall community.  In
a few cases, the closure of a plant may actually be viewed as a positive
net community effect (e.g., a small plant with a  high effluent load in an
area with a labor shortage).  These  impact factors will be qualitively
analyzed as appropriate.
                         G.   Other Effects
Other impacts  such as direct balance of payments effects will also be
included in the analysis.  This analysis too,  will involve qualitative
judgments.
                               IV-13

-------
      V.   POLLUTION CONTROL REQUIREMENTS AND COSTS
 Water pollution control standards, technology and costs used in this.
 analysis were provided by the Environmental Protection Agency.  The
 conclusions of this report are based on those costs.  During the prepar-
 ation of this report, a number of changes were introduced by EPA but
 it is believed by the contractor that the cost figures and investment
 amounts shown in the analytical portion of this report are current.
 Several factors,  however, have been spelled out in the limits to this
 analysis which bear specifically on the information and  cost as pro-
 vided by EPA.  Further,  it should be noted that the information shown
 below refers specifically to cane sugar refineries.  Sugar cane milling
 costs and impacts are not shown and are not to be considered at this  time.
                   Alternative Effluent Control Levels
General levels of pollution control for the cane sugar refinery industry,
both the liquid sugar segment and the crystalline sugar segment are set forth
below.  Each of these levels  indicate an effluent discharge and the loadings
for this discharge in BOD and Suspended Solids are shown in Table V-l.

        1.   Alternative A:  No waste treatment or control.  Essentially
            the effluent from this alternative is the raw effluent and
            there is neither treatment or cost involved with this  alter-
            native.

        Z.   Alternative B:  Elimination of discharge from filters.  This
            alternative can be achieved by either impounding the mud
            resulting from slurrying the filter cake with water or by dry
            hauling the desweetened filter cake to land fill.  B-l assumes
            that the  filter slurry is impounded and B-2 assumes  dry
            disposal of the filter cake.

        3.   Alternative C:  Inplant modifications to reduce entrainment
            of sucrose into conderiser water.   This alternative includes
            the installation of the demisters and external separators in
            order to reduce entrainment of sucrose in condenser water.
            In addition,  refineries have  good baffling and operation
            controls in the evaporators and vacuum pans as well as
            good vapor height.
                                V-l

-------
Table  V-l.  Summary of waste loads from effluent treatment alternatives
                          for cane sugar refineries

Liquid
BOD SS
Crystalline
BOD SS
i i at ;^ t^~
Alternative A
Alternative B-l
Alternative B-2
Alternative C
Alternative D
Alternative E - 1
Alternative E -2
Source: Development
3.43 1.56 1.54 1
3.25 1.00
3.25 1.00
2.90 1 . t 0
0. 24 0. 10
0.06 0.03
0.06 0.03
Document for Effluem
and Standards of Performance; Cane
of the Suga r
1.36 1.30
1.36 1.30
1.16 1. 30
0.38 0.06
0.04 0.03
0.04 0.03
Limitations Guidelines
Sugar Refining Segment
Processing Industry, Environmental Protection
A gency.
                              V-2

-------
        4.   Alternative D: Biological treatment of process watej-.   This
            alternative assumes  the use of an activated sludge plant to
            treat process water in addition to the  treatment under Alter-
            native B and C.  While there are presently no refineries which
            have their own biological treatment systems, the process waste
            water is highly bio-degradable and thus well suited for biologn al
            treatment in the  opinion of the Development Document as
            furnished by EPA.

        5.   Alternative E: Recycle of  condenser water and biological
            treatment of blowdown. This alternative includes, in addi-
            tion to Alternative D, the  recycle of condenser water followed
            by biological treatment of the blowdown in an activated sludge
            unit.  The blowdown  is to be approximately two percent of
            the total flow.  Recycle of  condenser water accomplishes
            two important things.  One, it cools the water, thus removing
            the heat normally discharged and,  (Z) it concentrates the waste
            loadings into the smaller blowdown stream, making biological
            treatment of this waste stream feasible.  Alternative E-l
            assumes a cooling tower.   Alternative E-2 assumes a spray
            pond.  Furthermore,  where the E technology is used in con-
            junction with Alternative D, a sand filter must also be  added
            at the end of the  line for removal of suspended solids.

Within the above context and water pollution abatement requirements
under the Federal Water Pollution Control amendments for 1972,  the
following three categories of. control we re evaluated.  Referring to
Table V-2, the three  levels of control  are Best Practical  Control Tech-
nology Currently Available, which is to be instituted by 1977, Best
Available Technology Economically Achievable which is to be instituted
by 1983, and  the New Source Performance Standards which will be in
effect for all  new  sources coming onstream by 1974.  From  the proposed
guidelines for liquid and crystalline refineries in the Development  Document,
all refineries need to achieve Level D  of the  alternatives for Best Practical
Control Technology Currently Available (BPT) by 1977 and Alternative  E
for Best Available Technology Economically Achievable (BAT) by 1983.

                   B.   Current  Level of Control
To identify current levels of control or inplace technologies refer to
Table V-3, which is a  listing of the methods of disposal of •waste water
at each refinery.   This listing is from the EPA Development Document for
Effluent Limitations Guidelines.  Although specific refineries cannot be
identified, refer to Table V-4 which indicates by Code Number, the type
of refinery,  its capacity, and its model classification.

                                V-3

-------
         Table V-2.   Proposed effluent limitations guidelines
                             BPT-              BAT-           NSPS^
                           BOD     SS       BOD     SS       BOD     SS
                            	kilograms per metric ton of melt	

Monthly average

     Liquid                  0.24     0.10      0.06   0.03      0.06   0,03
                          (0..48)!/ (0.20)     (0.12)  (0.06)     (0.12)  (0.06)
     Crystalline             0.38     0.06      0.04   0.03      0.04   0.03
                          (0.76)    (0.12)     (0.08)  (0.06)     (0.08)  (0.06)

Daily average

     Liquid                  0.85     0.45      0.21   0.14      0.21   0.14
                          (1.70)    (0.90)     (0.42)  (0.28)    (0.42)  (0.28)
     Crystalline             1.14     0 24      0.12   0.12      0.12   0.12
	(2.28)    (0.48)     (0.24)  (0.24)     (0.24)  (0.24)
—  Best practical control technology currently available -  1977.
2/
—  Best available technology economically achievable - 1983.

—  New source performance standards.
4/
—  Bracket figures  are pounds per ton.

   Source:  Development Document For Effluent Limitations Guidelines
            and Standards of Performance;  Cane Sugar Refinery Segment
            of the Sugar Processing Industry, Environmental Protection
            Agency.
                                 V-4

-------
    Table V-3.  Summary of wastewater treatment and disposal
         techniques of United States' cane  sugar refineries _L/
Refinery                      Disposal of Wastewaters

C-l           All process wastewater to municipal sewers; condenser
              water to river.

C-2           All process wastewater to municipal sewers; condenser
              water to river.

C-3           All liquid wastes to river.

C-4           All process wastewater to municipal sewers; condenser
              water to river.

C-5           All process wastes to municipal sewers;  condenser water
              to river.

C-6           All liquid wastes to river.

C-7           Primary settling of process wastes; all discharge to
              river.

C-8           All liquid wastes  currently to river.  Hook up to  municipal
               system  completed for process water and expected tobe
               ope rational before  1977.
C-9           Most process wastewater to municipal sewers; condenser
              water to river.

C-10         Most process wastewater to municipal sewers; condenser
              water to river.

C-ll         Discharge into  a swamp after traveling
              through  a two and a half mile canal.

C-12         Total impoundment of wastewater resulting in no  dis-
              charge to navigable waters.

C-13         Discharges into a  swamp.

C-14         All process wastes to municipal sewers;  recycle  of con-
              denser water through a  cooling tower  and discharge of
              blowdown to municipal  sewers.
                                V-5

-------
  Table V-3.  Summary of wastewater treatment and disposal
        techniques of United States' cane sugar refineries
                           (continued)
Refinery                     Disposal of Wastewaters

L-l           All liquid wastes to municipal sewers.

L.-2           All liquid wastes to municipal sewer; condenser water
              to river.

L-3           All process wastewater to municipal sewer; condenser
              water to river.

L-4           Total impoundment of wastewaters  resulting in no dis-
              charge  to navigable waters.
L-5           Discharge of process water;  cooling tower for condenser water
CL-1         All process wastewater to municipal sewers;  condenser
              water to river.

CL-2         Most of process wastes to municipal sewers;  condenser
              wate r to river .

CF-1         Closed system of canals and  holding ponds resulting in
              no discharge to navigable waters.

CF-2         Total impoundment of acid/caustic  wastes and filter
              cake slurry; impoundment with overflow of all other
              wastewaters.

CF-3         Condenser water  passed through spray pond (partial
              recycle possible) before discharge; all process waste-
              waters discharged to impoundage.

CF-4         Condenser water  impounded  then discharged; all other
              waters impounded completely in ponds; cooling  tower
              recently built.

CF-5         Partial impoundment.

CF-6         Partial reuse of wastewaters in raw sugar factory
              for  cane washings during grinding  season.

CF-7         Partial impoundment.

CF-8	Partial impoundment.	
Source:  Development Document for Effluent Limitations Guidelines and
         Standards of  Performance; Cane Sugar Refinery Segment of the Sugar
         Processing Industry,  Environmental Protection Agency.
                                V-6

-------
 Table V-4.  Cane  sugar refineries,  code, capacity and classification
Code
C-l
C-2
C-3
C-4
C-5
C-6
C-7
C-8
C-9
C-10
C-ll
C-12
C-13
C-14
L-l
L-2
L-3
L-4
L-5
CL-1
CL-2
CF-1
CF-2
CF-3
CF-4
CF-5
CF-6
CF-7
CF-8
Capa city
ton/day
2,600
2, 100
3,250
2, 100
1,000
190
3,500
1,500
2,000
1,200
1,500
350
1,700
2,200
300
800
850
390
100
1,800
820
460
700
660
700
220
600
400
700
Type of Refinery Classification _
Crystalline 4
4
4
" 4
4
2
4
4
" 4
4
" 3
" 2
11 3
4
Liquid 1
1
1 1
1
1
Crystalline-Liquid 4
4
Ref.-Mill 2
" 3
2
3
2
2
" 2
2
—  Classification refers to model segment:
        1  - Liquid
        2  - Small rural crystalline
        3  - Large rural crystalline
        4  - Urban crystalline
                                 V-7

-------
Table V-5 indicates the type and extent of treatment at each specific
refinery showing how the process water and the condenser water is
currently handled.  While it was not possible to translate each of the
descriptions of how the discharge was handled into specific alternative
levels  of technology, a close,  and we feel reasonable appraisal of the
inplace technology was made.   For each of  the cane  sugar refineries,
a designation of the current status of inplace control is  shown in Table
V-5.

From this table it  can be seen that 16 plants currently either discharge
their process water to  a municipal system  or have some other form of total
treatment  so that  there is effectively no discharge of effluent from the
process water to surface water bodies.  By the same analysis,  there
are only five plants that have either treatment for their conde:nser
water or discharge the condenser water to  a municipal system.  This
would indicate that treatment for condenser water is a major consideration.
Supportive of this  position is the fact that there are 14 plants that discharge
condenser water after making one pass through the  condenser.
               C.   Water Pollution Abatement Costs
The  costs of the various alternatives of treatment from B  through E
were furnished by the Environmental Protection Agency through Supple-
ment A of The Development Document for Effluent Limitations Guide-
lines.  Table V-6 shows a summary of these  costs for both liquid and
crystalline plants and shows the incremental  investment and annual cost
of operation  involved for each level of treatment.

1.   Investment
The figures on investment for each level of technology were used in total
as received and the conclusions, as far as the impact of costs shown in
the next chapter,  follow from these estimates.

The assumption was made that B-l or B-2 was in place for most refineries
and therefore, the investments for the  B-l or B-Z technology was used only
in evaluating one  refinery in Table V-7.  Similarly the need for Alternative
C technology, involving various entrainment devices for the vacuum pans
and the evaporators, was not clearly defined.   The amount of investment
for Alternative C appeared to be a small part of the total investment,  how-
ever, when compared to the D and E levels, therefore the lack of specific-
knowledge was not considered serious.


                                V-8

-------
Table V-5. Cane  sugar refineries, water effluent discharge status
Process Water Condenser Water
Code
C-l
C-2
C-3
C-4
C-5
C-6
C-7
C-8
C-9
C-10
C-ll
C-12
C-13
C-14
L-l
1.-2
L-3
L-4
L-5
CL-1
CL-2
No
Treat- Municipal
ment system
X
X
X
X
X
X
J./

xi/
xi/



X
X
X
X

X
X
X — '
Partial Total Direct dis- Partial Cool
Treat- Treat- charge to Municipal Treat- and
ment ment water bodies system ment Recycle
X
X
X
X
X
X
X X
X X
X
x
x!' x
X
X-J / If
— -A.
X
X
X
X
X
X
X
X
Total
Treat-
ment











X





X



                                                                          continued--

-------
                                Table V-5.   (continued)



Code
CF-1
CF-2
CF-3
CF-4
CF-5
CF-6
CF-7
CF-8
Process Water
No Partial
Treat- Municipal Treat-
ment system ment




X
X
X
X
Condenser Water
Total Direct dis-
Treat- charge to Municipal
ment watt.r bodies system
X
X
X
X




Partial Cool Total
Treat- and Treat-
ment Recycle ment
X
X
X
X
X
X
X
X
J7 Expect to be on municipal hookup by the end of 1973.
—I Most process water to a municipal system.
I./ Discharge to a swamp - not to a navigable river.

-------
Table V-6.  Cane sugar refinery water pollution control investment and annual costs —' by technologies

Liquid
Investment
Annual cost — '
j Crystalline
' Small
V—'
>— Investment
Annual cost _'
Large
Investment
Annual cost _'
— ' All costs updated
A
0
0
0
0
0
0
from
B-l
33.0
6.2
35.5
5.8
71.0
15.0
B-2
66.0
39.5
66.0
39.5
66.0
68.5
C
58.0
23.6
56.0
20.3
79.0
25. 1
1971 to 1972 by use of 1.076
—' Annual maintenance and operating cost les
_' Includes cost of sand filter.
Source- Development Document for Effluent
Cane Suga r
Refining Segment
D
E-l
	 $1,000 --
362.0 157.
145.9 18.
273, 0
127.6
712.0
169. 1
multiplier.
339.
46.
709.
109.

E-l!/ E-2
0 187.0 133.0
4 20.0 15.5
0 371.9 270.0
4 48.0 40.6
0 766.0 584,0
0 113.4 87.7

E-2!/
163.0
17. 1
302. 9
42. 1
640. 0
92. 1

s depreciation and interest.
Limitations Guidelines
of Sugar Processing Industry
and
Standards of Pe rformance;

- Supplement A , Cost Analysis .
      Environmental Protection Agency

-------
Table V-7.  Cane sugar refineries estimated technology needs and costs to meet best practical control technology
                                       currently available
Code
C-l
C-2
C-3
C-4
C-5
C-6
C-7
C-8
C-9
f C-10
K c-n
C-12
C-l 3
C-14
L-l
L-2
L-3
L-4
L-5
CL-1
CL-2
B-li/ B-2 L1
Capacity Invest- Annual Invest- Annual
ton/day ment Cost ment Cost

2,600
2, 100
3,250 71 . 15.0
2, 100
1,000
190
3,500
1,500
2,000
1,200
1,500
350
1,700
2,200
300
800
850
390
100
1,800
820
C
Invest-
ment
__ "ROOD



56
79
79
79



58
58
58
56

Annual
Cost




20.3
25. 1
25. 1
25. 1



23.6
23.6
23.6
20.3
D
Total
Invest- Annual Invest- Annual
ment Cost ment Cost


711 169.1 782

273 127.6 329
711 169.1 790
79
79
711 169.1 711
711 169.1 711


58
58
362 145.9 420
56


184. 1

147.9
194.2
25. 1
25. 1
169. 1
169. 1


23.6
23.6
169.5
20.3
                                                                                               continued--

-------
                                           Table V-7 (continued)
Code
CF-1
CF-2
CF-3
CF-4
CF-5
CF-6
CF-7
CF-8
Totals
No. of
B-l17 B-21/
Capacity Invest- Annual Invest- Annual
ton/day ment Cost ment Cost

460
700
6 660
700
220
600
400
700
71 15.0 0 0
Refineries 1 0
C
Invest-
ment
- -tni

56
56
56
56
56
56
56
915
15
Annual
Cost
~\n __ _ .

20.3
20.3
20.3
20.3
20.3
20.3
20.3
328.8

D
Invest-
ment





273
273
273
273
4,571
10
Annual
Cost





127.6
127.6
127.6
127.6
1,460.3

Total
Invest-
ment


56
56
56
329
329
329
329
5,557
18
Annual
Cost


20.3
20.3
20.3
147.9
147.9
147.9
147.9
1,804. 1

—  Arbitrarily B-l costs we assumed for rural and B-2 costs for urban refineries.

-------
Table V-7 taken in total shows  the various refineries that require invest-
ment and expense to meet the BPT level and Table V-8 shows what in-
cremental investments and expenses need to be made by 1983 in order
to achieve the BAT level of control.

2.   Operating and Ownership Costs

In contrast with the beet sugar  industry, for example, operating and
maintenance costs are a significant part of the total  costs of water
pollution control equipment and practices as compared to the total
cost of investment.  As will be seen later, the amount of annual ex-
pense does have a significant impact on the refineries and the results
of the discounted cash flow analysis.  Annual depreciation charges of
five percent were taken on equipment on the  presumption that this
equipment would have a 20-year life and no salvage value.

3.   Estimated Costs
Based on the data which have been described above,  it was possible to
make a total cost estimate for each  refinery.  For the purposes of
the impact analysis this cost information was then blended in with each
model plant in order to measure  the impact on a plant by plant basis.
Overall on the industry wide basis for the BPT level of treatment,  a
total of $5,557,000 would need to be invested.   For the BAT Level, this
investment is an additional $11, 120, 000.

These costs,  as  previously mentioned, assume that the levels  of tech-
nology specified  will produce the  level of treatment required to meet
the guidelines and, secondly,  that the alternatives of treatment are
properly costed  so that these do, in fact,  represent actual dollars  to
be spent by each refinery. Of the 29 refineries,  18 will be required to
invest money by  1977 and a total  of 22 will be investing in water pollu-
tion control by 1983.
                                 V-14

-------
Table V-8.   Cane sugar refineries estimated technology needs and costs to meet best available technology
                                  economically achievable - 1972 data
Cocki

C-l
C-2
C-3
C-4
C-5
C-6
C-7
C-8
C-9
C-10
C-ll
C-12
C-13
C-14
L-l
L~2
L-3
L-4
L-5
CL-1
CL-2
Capacity
ton/day

2,600
2, 100
3,250
2, 100
1,000
190
3,500
1,500
2,000
1,200
1,500
350
1,700
Z.200
300
800
850
390
100
1, 800
820
E-
Invest-
ment


709
709
766
709
709

766
709
709
709





157
157

28
709
339
-i-i' E-zi'
Annual Invest- Annual
Cost ment Cost
_ __
-------
                                        Table V-8 (continued)
V 1 ll TT ? l>
ii- i — Cj-i, —
Code
Capacity
ton /day
Invest- Annual Invest-
ment Cost ment
Annual
Cost
Invest-
ment
Total

Annual
Cost
. 	 _ _ 
-------
                     VI.   IMPACT ANALYSIS
The impacts considered in this analysis include the following:

       Price effects
       Financial effects
       Production effects
       Employment effects
       Community effects
       Balance of payments effects

A comprehensive and detailed analysis of each of the above was beyond
the scope of this study.   Consequently,  efforts were allocated more to
the financial and plant closure analysis  with lesser effort on the other
macro-economic impacts.
                         A.  Price Effects
Estimated price increases  necessary for the industry to maintain its
current level of profitability are not large,  although certain segments
will require much hi her increases than others.  Table VI-1 shows
estimated price increases  required to maintain estimated current
profitability levels based on the model plant analysis.  It shows the
incremental increases involved in the BPT  level, the  BAT level, and
the total of both, which would be required by 1983.

Except for the segment of refineries listed  as small rural, all price
increases needed are  less than one percent.  The liquid plants need the
least price  increase,  only  . 14 of one percent.   The small rural plants,
and this  is only some  of the plants in this group,  show a need for 2.07
percent increase while the  large rural is . 92  of one percent and the
urban plants require .61 of one percent increase.  Actually, five plants,
which require no treatment costs whatsoever  represent 11 percent of
the total refinery capacity and would show in this table to need a zero
price increase.

In the case  of the sugar beet industry, a larger percent of the total
industry was not required to spend money for water pollution control
due to the fact that they were operating at zero  discharge already.
This  percentage was approximately 30 percent.  In the case  of cane
sugar, only 11 percent of the industry is  currently meeting both  the
1977  and 1983 guidelines.  On the  other hand, the need for price increases
and the amount of price impact in cane sugar  is about the same as  the beet
sugar industry.
                                VI- 1

-------
    Table VI-1.  Percentage price increases needed to maintain profitability
                        BPT               BAT        Total increase by '83
  Model	Min.   Max.	Min.   Max.	Min.     Max.

Liquid                 0        0          0.14           0      .14
Crystalline
   Small rural         0     1.74          0     . 33           0     2.07

   Large rural         0      .68          0     .24           0      .92

   Urban               0      .44        .16     .16          .16      .61
                                  VI-2

-------
Since the demand for sugar at the household level is  relatively inelastic,
we doubt that such price increases would alter this consumption pattern
significantly.  Although price elasticities for  industrial users and cross
elasticities with other sweeteners,  such as beet sugar,  corn sweeteners,
and synthetics, are not known with certainty,  there appears to be a possi-
bility that sugar itself, both beet and  cane, could become less  competitive.
Because of this price pressure, it may be  that some  companies will with-
draw from specific markets in which  they  compete at a  disadvantage and
thus independently find ways and means of satisfying their own need for
price increases.  A recent example noted  in the press was that of Holly
Sugar,  a beet  sugar company announcing it was withdrawing from the
Chicago market sinc<-  they did not have enough sugar to compete  in all
markets and the Chi. ago market paid the lowest price.

However,  under present legislation, sugar's ultimate competitive position
will depend upon the Department of Agriculture's policy regarding such
costs and  how these are interpreted in relation to import quotas.  Objectives
of the Sugar Act, dif- ussed in Chapter III, suggested that pollution  control
costs could receive  • ome  consideration', but again it needs to be  pointed
out that it is strictly at the option of the  Secretary to act under broad
powers  rather than specific powers in the  Act.

The Act in Section 2n5 entitled "Allotments of Quotas or Prorations"
states that the Secretary of Agriculture shall  make allotments  to assure
an orderly and adequate flow  of sugar to prevent disorderly marketing
or importation,  and o maintain a continuous and stable supply of sugar so
as to afford all interested  persons an equitable opportunity to market
sugar.   It seems tha • , under  this  section,  the Secretary could make
adjustments in quotas  to adjust for  increased  costs of pollution.  However,
in doing so, it is suspected that the Secretary would  take into account
the cost of impacts of pollution control in both the  beet  and cane  sugar
industries.  In doing so the Secretary could be  constrained to variances
in the price of some three or four  percent, as defined in Section 202
of the Act.

Thus, an important factor for price changes in response to the imposition
of pollution controls appears  to be the position which the Secretary chooses
to take.  It is  of interest to note that some members  of the sugar industry
believe the Secretary  is not taking full advantage of his  powers to insure
their welfare.  However,  some professionals who  have  studied the United
States sugar policy have suggested  that the benefits of a domestic sugar
industry are considerably less than the cost of maintaining this industry
                                 VI-3

-------
and that policy be redirected in favor of increased imports.  Given the
current posture  toward the removal of government agricultural controls,
it seems that a ruling by the Secretary  in favor of increased prices for
the domestic sugar industry can not be automatically expected.

Satisfaction of one purpose could also be in conflict with another.  In
view of current pressures to keep food prices down, the provision of
ample  sugar supplies at reasonable prices might well receive  greater
weight than  other purposes.

Current price ceilings due  to wage arid price < ontrols have tended  to
hold down any normal price increases whi« h might be expected in the
entire  sweetener industry.   With the termination of such controls or
allowable adjustments,  there will probably be some movement of prices
upward due  to the depressed earnings of the  entire suyar industry.

It is felt, however, that price iru reaves specifically Beared to v/ater
pollution control  costs are  not possible  under I he-  existing conditions of
the Sugar A
-------
Present values were computed using both a 6  1/2 percent and a 7 1/2
percent discount rate, which is the approximate after-tax cost of capital
(equity and debt) in the cane sugar refinery industry as was  shown in the
computation in Chapter V.  A higher rate would make these  impacts more
severe and a lower rate would reduce the impacts.  In these terms, present
value of cash flows, after adding pollution control costs, show a significant
financial impact with either discount rate.

In order to apply the discounted  cash flow procedure  to the sugar re-
fineries, certain steps have been taken.   First of all the costs of various
alternatives of water pollution control--both investment and annual oper-
ating costs--have been applied to specific model refineries.  Discounted
cash flows, assuming a  6.5 percent and a 7.5 percent rate after taxes ,
were computed for two cases--before (Base case) and after  (BPT and
BAT) were computed for pollution control.

The  results of these  runs are shown in Table  VT-2.   The specific costs
for each level of treatment technology were taken from Table V-7  for
BPT and V-8 for BAT.  Water pollution control costs from these tables
varied from zero to as much as  $790,000 for  the C-7 refinery for 1977
BPT guidelines.  For the BAT 1983 proposed guidelines, the incremental
costs varied from zero to $766,000.

It was the costs from Tables V-7 and V-8,  added to the  appropriate
model base case that resulted in Table VI-2.  Refineries that had  zero
costs show no impact.  Refineries such as C-7 that needed Alternatives B,
D and E-l  that show an impact by having the net present value of a targeted
discounted cash flow of 6. 5 percent drop from $3, 949, 000 before pollution
control costs to a negative  amount.  This negative number indicates that
the model plant, when impacted  by costs of pollution control, refinery,
cannot maintain a cash flow that will meet its or the  industry's profit
targets.

Approximately 30 percent of the total capacity of the industry does show
some impact from the costs of these levels of control.  The total impact
on these plants will be discussed in the next section.  Further examination
of the data in  Table  VI-2 indicates that the cost required to  institute treat-
ment alternatives, E-l or E-2,  for condenser water has an impact on all
refineries.  From Table V-8 it  can be seen that 23 of the 29 plants will have
to make an investment in condenser cooling tower or spray  pond,  but
probably more significant is  the annual maintenance  and operating costs
that will be expended each year.  Annual maintenance and operating costs
over $100,000 per year are significant and markedly affect  the current
net values.
                                VI-5

-------
              Table VI-2.  Discounted cash flow for model refineries impacted with water pollution
                                          control costs from specific refineries
A Ite rna tive
Needed 1'

Liquid
Liquid
2/
S.— Crystalline
S. Crystalline
S. Crystalline
2/
LT C rystalline
L. Crystalline
I-H L. Crystalline
L. Crystalline
L. Crystalline

c.
C

Rural C,
Rural C,
Rural C,

Rural C,
Rural C,
Rural D,
Urban E-
Urban C,

E-l


D.E-1
E-l
E-l!/

E-2
E-l
E-2
1
D.E-1
Base
6.5

1,345
1, 345

701
701
701

1,849
1.849
1,849
3,949
3,949
7.5

892
89?

170
170
170

681
681
68i
2, 076
2,076


1
1

(1



1
1

3
2
BPT
6.5
	 $000
,037
,037

,258) (1
421
421

,569
,569
(725) (i
, 949 2
,786
BAT
7.5

604
604

,666)
(93)
(93)

418
418
,734)
, 076
(693)
6


1

(1



1
1
(1
1

.5

815
, 009

,724)
(100)
421

, 132
, 309
,734)
, 019
(208)
7.5

402
578

(2,095)
(568)
(93)

20
179
(2,674)
1, 015
(1,812)
Refineries requiring pollution control investment TOTAL
Refineries with no pollution control
Refineries with negative
cash flow,
required
therefore



not considered in this




analysis
Percent of
total production

4
1

1
2
2

2
2
9
38
22
83
11
6
—  Costs are for levels of technologies per Supplement A of Development Document Effluent Limitations
   Guidelines.
?L/ S = Small; L = Large

—  Needs only  sand filter.

-------
2.   Capital Availability Level

As  discussed in Chapter II, the cane sugar  refining industry as a whole
appears to be hard pressed to attract new capital.   Imposition of new
capital requirements,  particularly for non-productive assets, would appear
to be a problem for the entire industry.  However,  as previously pointed
out, this problem does  not appear to be more significant for any particular
segment of the  industry but is going to depend upon a company by company
analysis of its individual earnings.  The health of an individual company
and its ability to operate profitably,  or at least to  show performance
ratings superior to  other plants in the  same group, rests with its  current
competence of management, its past management philosophies ,  and the
degree of cost consciousness  which management has been able to instill
in its employees.
                      C.   Production Effects
Of critical and fundamental interest is the  production impact which the
cost of pollution control may cause.   This  effect is shown graphically by
looking at the results of discounted cash flows  and estimating the potential
plant closures due to the impact of costs of water pollution controls.  As
discussed in Chapter IV, the methodology used was  to apply shutdown models
to represent plants and to compare the appropriate model plant results
•with each of the firms in the cane sugar  refining industry and thus d raw
inferences for each based on its relationship to the model.

1.   Potential Plant Closures
Present values were computed at 6. 5 and 7. 5 percent after tax cost of
capital for each of the  models as  shown in Table VT-2.  Referring to
Table  VI-3,  impact, as shown by the discounted cash flow analysis has
been put into a table and evaluated on the basis  of this impact along with
many other possible closure factors.  In this way a plant by plant analysis
was made.  In interpreting discounted cash flow columns in this table, we
have shown L for low impact, M for moderate impact and H for high impact.
In other words, those with an H could be considered highly likely to close
if this  matter of discounted cash flow were the only criteria to be  measured.
Were that the case, the values of discounted  cash flows  which are less than
zero would indicate that the firms would be financially better off by liqui-
dating the sunk investment and reinvesting the money where it would yield
the industry's target return.  However, as indicated, there are other
factors to consider and it is a matter of judgment as to the parameters
and the weight to be given to each parameter when making statements
regarding potential plant closures.

                                 VI-7

-------
              Table  VI-3. Factors considered in cane sugar refinery closure analysis
i
co
Code
C 1
C 2 •
C 3
C 4
C 5
C 6
C 7
C 8
C 9
C 10
Cll
C 12-'
C131/
C 14-
11
L 1-
L2
L 3
L 4— '
L 5
CL 1
CL2
CF I-'
CF 2
CF 3
CF 4
Capacity
TPD-
2,600
2, 100
3,250
2, 100
i, ooo
190
3,500
1,500
2,000
1,200
1,500
350
1,700
2,200

300
800
850
390 •
100
1,800
820
460
700
660
700
Ownership
type
Multiplant
Multiplant
Multiplant
Multiplant
Multiplant
Integrated
Integrated
Single
Single
Single •
Multiplant
Multiplant
Single
Multiplant

Multiplant
Single
Multiplant
Multiplant
Integrated
Single
Multiplant
Integrated
Integrated
Integrated
Integrated
Integrated Rural
with mill Urban
U
U
. U
U
U
X R
X U
U
U
U
R
R
R
U
•
U
U
U
R
X R
U
U
X R
X R
X R
X R
Winter Market
climate advantage
Mod. 0
Severe 0
Mild 0
Mod. . 0
Severe 0
Mild +
Mild
Mild
Mod. 0
Severe 0-
Mild
Mild
Mild
Mild

Severe +
Severe +
Severe +
Mild
Mild +
Severe +
Severe +
Mild
Mild
Mild
Mild
Discounted cash flow
Base
L
L
L,
L
L
M
L
L
L
L
M
M
M
L

L '
L
L
L
H
L
L
M
L
M
L
BPT
L
L
H
L
I,
H
H
L
L
L
H
M
H
L

L
L
L
I,
H
L
1,
M
L,
•M
I,
BAT
L
L
H
L
L
H
H
L
M
M
H
M
H
L

L
L
L
L
H
M
M
M
M
M
L
                                                                        continued	

-------
I/
       Table VI-3.  Factors considered in cane sugar refinery closure analysis (continued)
Code
CF 5
CF 6
CF 7
CF 8
Capacity
TPD
220
600
400
700
Ownership
type
Integrated
Integrated
Integrated
Integrated
Integrated
with mill
X
X
X
X
Rural
Urban
R
R
R
R
Winter
climate
Mild
Mild
Mild
Mild
Market Discounted cash flow
advantage Base
+ H
+ H
+ H
+ H
BPT
H
H
H
H
BAT
H
H
H
H
—  Eleven percent of total refinery production now has no effluent discharge except to municipal sewage system.
   vO

-------
In Table VI-3 the  code for each plant is listed along with its capacity.
In evaluating a specific plant,  the capacity of the actual plant as com-
pared to the capacity of the model does give  some indication of its vul-
nerability to closing based on  capacity.  It is assumed that a  plant that
is larger than the model would be somewhat  less impacted than a plant
that was smaller than model. Two examples that were considered were
C-3 and C-7.  Both of these are ranked first-second in the industry
as far as capacity is  concerned and are substantially over the capacity
of the urban model (2,000 tons per day).  At the  other end of the scale,
there is the greater impact on the plant C-6  which has only a 190 tons
per day capacity as compared to the small refinery  model with 400 tons
per day.

Ownership type  was also  considered in the plant  analysis closure.  For
example, a single plant and a  single company seems to be more vulnerable
to closure  than would be a plant which is integrated  with a. mill, since  the
combined operation would be  considered when evaluating the plant in terms
of closure.  In a case of a multi-plant operation, the resources of a com-
pany that has  severla plants are usually greater  than a single plant and,
thus,  make it less vulnerable  to closing.  Also a case  can be made for
closing one plant of a multi-plant operation on the basis that production
could be consolidated or transferred to another  unit with expanding output.

As previously stated, those  refineries that are integrated with a mill
would seem to have a higher resistance to closing than those not inte-
grated.

Whether a  plant is a rural or a city refinery has its greatest significance
in the area of costs and thus shows up in the DCF analysis. However,
there seems to be no particular case where a plant  in an urban area is
more or less  vulnerable than a plant in a rural area just on the basis  of
its location.

The winter climate is somewhat of a factor in the closure analysis because
the major cost impact on all refineries is  the treatment of the  condenser
water.  Those plants which will be  required to operate cooling towers or
spray ponds have a particular problem where they are located in an area
•with severe winters as compared to those  plants that are located in mild
climates.  Operating a cooling tower in freezing weather is hazardous and
has a higher cost factor than operating one in year-round mild weather.

Another factor to consider  is what we have termed "market advantage'1 on a
plus, minus,  or zero basis.   Those plants that have some  advantage in their
market in that they are the only refinery in the area and don't have the cost
competition of other  refineries should have a higher price  potential than the
                                 vi-io

-------
model plant would.   For example,  one plant which may be impacted from
costs of water pollution control and penalized for  its small size,  never-
theless, does have a real advantage in its market compared with any other
refinery located hundreds of miles away.  By the  same token, a refinery
operating in Chicago would  seem to have a market advantage, by virtue
of its being located there  rather than having to ship  its sugar to this
larger market.  On the other side, those plants that are located away
from the market and require absorption of freight and other costs seem
to have a market disadvantage and thus are rated  with a minus factor.

Referring now to the columns which deal with DCF analysis,  we find  that
the refineries  of Puerto Rico are  shown to be highly impacted in the base
case before pollution control money is spent  and at the BPT and the BAT
level as well.  It has been difficult to  evaluate these plants since  we feel
that the Commonwealth of Puerto Rico is subsidizing them and it is diffi-
cult to anticipate to what degree subsidization in the future will continue.
On the other hand, faced with the  costs 
-------
 Twenty-three of the 29 plants therefore,  based on the information,
 costs, and other conditions previously stated, would, at this point,
 appear to have a low impact and a low likelihood of closure.  Those
 plants that are highly impacted represent 10 percent of the  number of
 plants (3) and 6 percent of productive capacity (2020 TPD).  Plants
 which are moderately impacted represent another 10 percent  of the
 plants (3) and an additional 6 percent of production (2090 TPD), and
 those plants least impacted represent 80  percent of the plants  (23) and
 88 percent of the production (30,580 TPD).

In looking into the production effects that  are  caused by events  described
above, it is seen that two to three  plant closures are in Puerto Rico
 representing two percent of the production.

 This 2 percent production can easily be absorbed by other Puerto Rican
 refineries as they have unused capacity.

 The  10 percent balance of lost production is on the mainland U.S. There
are no prospects for new refining  construction due to low industry earnings
and all refineries are  operating at essentially total or full capacity.

It is speculated that the following events might therefore take place:

       (a)   Domestic  raw sugar now going to  a closed refine ry would
            be  diverted to another refinery and the import quota lowered
            by ten pe rcent.

       (b)   The ten percent cane sugar loss might be made  up by beet
            sugar if beet sugar production can be increased in the face
            of water pollution  costs in that segment.

       (c)   Substitute  sweetners might take over the ten percent loss
            as  both  caloric and no caloric sweetners are expanding their
            share of the sweetner  market rapidly.
                             VI-12

-------
2.  Sensitivity Analysis

As  shown above, the impact of pollution control costs on potential
plant closures is believed to be moderate.  However, should pollu-
tion control costs differ from  those used in the analysis, the expected
impact would  likely be changed.  To gain an insight into the magnitude
of such changes, an evaluation of Table  VI-2 along with pollution con-
trol costs will form the basis  of a sensitivity analysis.

As  a point of  reference, key data from Tables VI-2, V-7 and V-8 are
displayed in Table VI-4 by refinery model.  As  can be seen, an addi-
tional investment of $156,800  and $18,400 O&M costs in pollution control
in liquid refineries  reduces the net present value  by $200,000.  For
type 2 plants, a small investment of $56,000 and $20,300 O&M costs
reduces NPV  to below zero.  In the case of the model No.  3 units (large
rural),  an investment of only $270, 000 reduces  NPV by $400, 000.  This
suggests that  an additional $100, 000 to $150, 000 investment and associ-
ated O&M costs would reduce  NPV to zero,  suggesting possible closure.
A similar pattern exists for the model No.  4 plants (urban),  although the
absolute level of investment is greater.

These data could be plotted and additional indicative analyses performed
in order to assess possible impacts of differing control Ivels and costs.

The essential point is that imposition of more strict BPT and BAT
standards, with presumably higher costs, could quickly lead to a
much higher potential closure rate.  The ultimate effect would, of
course, depend  on the magnitude of the additional costs. However,
given typical  cost-level of control relationships, one would conjecture
that stricter standards in  the cane sugar industry would dramatically
increase the rate  of potential closures in this industry.
                     D.   Employment Effects
Cane sugar refineries do not employ large labor forces for the size of
their output when measured in dollars  or tons.  The small refinery
would employ as'few as  32 full time people and the large refinery might
employ seven or eight hundred people.  Within this  group there are both
unskilled workers involved largely in handling sugar, loading and un-
loading, and operating materials and handling equipment.  The technicians
that are involved in actually operating the plant would be highly skilled and
years of experience would be required on their part.
                                VI-13

-------
   Table VI-4.  Sensitivity of model net present values to effluent
                          treatment costs

Type
Refinery


1
1
2
2
2
2
3
3
3
4
4
4

Net Present
Value Before
Impact


892
892
170
170
170 I/
•*• /
681
681
681
2,076
2,076
2,076
Effluent
Investment
	 
-------
                      E.   Community Effects
Community effects due to closures are more difficult to assess.  In the
urban areas,  the impact of sugar plants would be relatively small due to
the fact that the employment and tax dollars lost would  be the measure of
the impact.  The loss of value of raw material which is usually imported
or shipped a long distance by a domestic industry would not be felt locally.
In the case  of rural plants where refinery is located in  conjunction with
a raw sugar cane  mill,  community effects would be greater.  In these
areas sugar is a prime  industry and its effects would be felt throughout
the area from the refinery to the mill to the sugar cane grower.  The
impact of closure as shown in "Production Effects" would indicate that
3 to 6 small communities might be affected.
                  F.  Blance of Payments Effects
With the implementation of discharge controls, it has been shown that
6 to 12 percent of the cane sugar refinery capacity may be impacted
sufficiently to  close.  Were this to happen, the refining of sugar could
be shifted as discussed in "Production Effects" to:

       (a)   Other expanded  cane sugar refineries
       (b)   Beet sugar production
       (c)   Importation of refined sugar

If (a)  or  (b) did not happen due to any number of factors such as the
weather  or  lack of availability of other production facilities, then the
increase in foreign imported refined sugar would adversely affect the
balance of  payments.   This would  be of particular concern at present
since every effort is being made by government to improve the balance
of payments.

At this time it is not known what effect the  guidelines will have on beet
sugar production although the construction  of new beet sugar plants and
resulting new production should offset the loss of production due to the
closure of impacted plants.   No new cane sugar refineries have been
built for many years and it is doubtful if they will be now.
                                VI-15

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The possible expansion of the current refineries is the most likely
event and,  therefore the balance of payments effects should be minimal.
One question not yet answered is the impact of pollution control costs on
sugar cane mills.  Should this segment be impacted and domestic raw
sugar production lost, adjustments by the Secretary of Agriculture
would undoubtedly take place to increase the flow of imported raw sugar.
Such an event would create a balance of payment effect of adverse con-
sequences .
                                VI-16

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                       VII.  LIMITS TO ANALYSIS
                          A.  General Accuracy
Data gathered were of secondary nature drawn from previously published
reports, from private sources, contracted government studies and regular-
ly reported government services.  Personal interviews of key personnel
of refinery and sugar cane milling companies  and trade associations were
conducted.

Throughout the study an effort was made to evaluate data  and other infor-
mation used and to update these materials, wherever possible.  Data were
reworked so as to make, its presentation more clear in light of the purpose
of this report and to the use that is intended.

As a result of the data and the step by step methodology by which  the con-
clusions are drawn,  this analysis represents a systematic evaluation of
the impact of effluent limitation guidelines on  the cane sugar refinery
industry.  However,  it must be recognized that judgements based on this
data are not absolute and the estimates  represent the best relative conclu-
sions given the limitations of time and budget.
                       B.  Possible Range of Error
 The instructions of the contract required that the contractor use the cost
 data  provided by EPA  under Supplement A of the Development Document.
 The following items indicate some of the range of error that is possible
 based on the use of the data  supplied by EPA and the basic financial data.

Different data series and different sections of the analysis will have
different possible ranges of error.  Estimated error ranges as an order
of magnitude are as follows:

                                                    Error Range

       1.    For number,  location,  capacity,
             and processes of plants                     _+0. 2%

       2.    Price information on products,
             materials and equipment                    -10.0%
                                VII-1

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       3.   Sunk investment

       4.   Plant operating costs

       5.   Land values

       6.   Pollution

       7.   Plant closures
   Error Range

       J- 20. 0%

       _+ 10.0%

$1,000  - $100,000 acre

       _f 50. 0%

        + 15.0%
                        C.   New Technology
Two new technologies, not evaluated,  \vhith have potential impacts on
waste water disposal are  in the ea rly  stages of i ons i do ration or use by
the industry.  One is the condensation of sugar vapor by Compression
rather than by cooling  in a i onden.st- r.   This toi hnolo -j.} , not fully de-
veloped for application to cane sugar, is of interest,  bciause it elimin-
ates the need for large volumes of water lor Condenser tooling and,
thus the entrainment of sugar in the cooling water.

The principle involves the use of a  compressor for compressing the
sugar vapor into liquid.  Energy  is required to accomplish this but a
by-product of the  process is that the heat generated in the compressing
phase can  be used  as heat ene rgy in the total suga r refining p rocess .

"Dry cooling towers"  which eliminate or reduce fog producing and air
polluting tendencies are under development.  Little data concerning
them is known at this  time except that both the investment cost and
operating expense  may run 3 times the figures of  currently operating
"wet cooling towers."
                                 VII-2

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                     D.   Critical As sumptions
A key assumption in the analysis concerns the action of the Department
of Agriculture in response to maintaining the health of the sugar industry.
The Secretary of Agriculture can act on certain conditions which include
maintaining orderly marketing and supply processes.   Further, under
the broad terms of the Sugar Act,  there are  provisions to assure an
equitable division of returns from sugar between beet and cane growers,
farmworkers and processors.  However,  it is unknown as to whether or
how the Secretary would act in response to added  costs to the processors
arising from pollution control requirements.

Those  refineries now  on municipal hookups are dependent upon two
assumptions:  (a) that user charges for the future will be within pre-
dictable limits and be  economically affordable by  refineries; (b) that
no forms of pre-treatment for refineries in the future will be required.

A final  critical assumption lies in the  reliability of the cost data and
the contractor's ability to project  by models these cost data.  Care has
been taken in  working with these data but without access by the contractor
to financial information of specific refineries, necessary assumption of
costs have had to be made.
                     E.   Remaining Questions
One question for cane sugar refineries  concerns the impact on sugarcane
mills.  The mills' water pollution problem is more difficult by a factor of
at least 2 than that of the cane sugar refiner.  The ultimate impact on many
refineries may depend  on the impact of pollution controls on the mills.
This is due  to both the  integrated ownership  of mills and refineries and the
location proximities  of mills and refineries.

Further questions depend on costs, adequacy of treatment technology,
and relations with municipal sewage systems alluded to in the previous
section.
                                VII-3

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 BIBLIOGRAPHIC DATA
 SHEET
                     1. Report No.
                        EPA-230/1-73-003
4. TK!C and Subtitle  Economic Impact of Costs of Proposed Effluent
  Limitation (guidelines  for the  Cane Sugar Refining Segment of
  the Sugar Processing Industry
3* Recipient's Accession No.
                                                                     5. Report Date October, 1973
                                                                       Date of completion
                                                                     6.
7. Author(s)
          Milton L. David, Robert!. Buzenber^
                                                                     8. Performing Organization Reft.
                                                                       No.   122
9. Performing Organization, Name and Address
  Development Planning and Research Associates,  Inc.
  P. O.  Box 727
  Manhattan,  Kansas  66502
                                                                     10. Protect/1 ask, »ork Unit .No.
                                                                        Task Order No.  5
                                                                     11. Contract/Grant No.
                                                                        Contract No.
                                                                        68-01-1533
12. Sponsoring Organization Name and Address
 Environmental Protection Agency
 Waterside Mall
 4th and M Streets, S.W.
 Washington, D. C.  20460
                                                                     13. Type ot Report & Period
                                                                        Covered
                                                                        Final Report
                                                                     14.
15. Supplementary Notes
16. Abstracts      The  cane sugar refining segment of the  sugar industry (SIC 2062)  is com-
 posed of 29  refineries operated by 20 companies.  Most refineries, though over 50 years
 old, have been modernized and operate at full capacity refining raw sugar -- 32 percent
 of domestic  sources  and 68 percent  imported.  Two companies purchase 45  percent of
 the total capacity.  Estimated after-tax return on sales are about one percent for all
 sizes of liquid and crystalline refineries.  Prices are controlled indirectly under the
 Sugar Act by adjustments in the  supply by the Secretary of Agriculture.  There is
 price competition from other sweeteners.
                Imposition of effluent limitations are not expected to raise prices.
 Potential refinery closures by 1977  due to the imposition of the effluent limitation guide-
 lines are estimated to be from three to six refineries representing from six to twelve
 percent of total production.  No  additional closures by 1983 are expected.
17. Key U'ords and Document Analysis.  17a. Descriptors
 Pollution, wite r pollution,  industrial wastes , cane sugar,  sugar refineries,  economic,
 economic analysis,  discounted cashflow, demand, supply, prices, fixed costs, variable
 costs, community, production capacity,  fixed investment
17b. Identifiers/Open-Ended Terms
17c. CP
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16.  (continued)

       Employment and community impacts appear to be small.  The
impact analysis is based on a number of assumptions and cost estimates
which are identified in the report.

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